KR101129826B1 - A carbonization system and the carbonization vehicle for processing all kinds of wastes - Google Patents

Abstract

Industrial Applicability The present invention is directed to an indirect heating type carbonization system for waste that collects and effectively carbonizes and treats organic polluted industrial wastes, livestock wastes, and medical wastes discharged from various industries, livestock industries, and medical related industries, and carbonization vehicles using the same. A carbonization furnace main body, a carbonization chamber embedded in the carbonization furnace body and closed by external air, and a heat flow passage excluding the front surface where the door portion of the carbonization chamber is formed are provided. Hot air generated in the burner circulates, and provides a structure in which a discharge pipe for discharging combustion gas and hot air from the hot flow path is formed. The heat flow path provided in the indirect heating type carbonization treatment system of the present invention has a double wall structure surrounded by the inner wall and the outer wall of the carbonization chamber, and the space between the inner wall and the outer wall has a serpentine type structure. It has a large number of partitions to partition and is arranged to surround five sides except the door part (waste inlet) of the carbonization chamber so that the hot air is discharged after circulating the entire carbonization chamber to improve heat conduction efficiency and energy. Consumption can be greatly suppressed.
According to the present invention, carbonization of waste generated in various industries, animal husbandry, and medical related industries is performed by carbonization near the site of generation or continuously during the movement of a vehicle, thereby effectively carbonizing the waste without effectively polluting the surrounding environment. Effect is obtained.

Description

A CARBONIZATION SYSTEM AND THE CARBONIZATION VEHICLE FOR PROCESSING ALL KINDS OF WASTES}

The present invention is an indirect heating type carbonization treatment system for wastes that collect and effectively carbonize and treat organic polluted industrial wastes, livestock wastes and medical wastes discharged from various industries, livestock industries, and medical related industries. It relates to a carbonized vehicle equipped.

Generally, a large amount of waste (hereinafter referred to simply as "waste") is disposed of in various industries, animal husbandry, sewage treatment plants and medical institutions.

Such waste was recovered by a collection vehicle, and landfilling or incineration was a common treatment method.

However, in the process of incineration of such wastes, since a large amount of harmful substances such as taioxin are emitted to cause environmental pollution, the disposal of wastes is a problem both internationally and socially.

In particular, incineration of waste is not only in advanced countries but also in developing countries, which are experiencing rapid economic growth, and the restriction on emission and recycling of waste is urgent.

On the other hand, carbonization is a treatment method in which wastes and the like are indirectly heated in an oxygen-free state using a carbonization furnace to thermally decompose components other than carbon and collect them as fixed carbon for resourceization.

Although there is still a small amount of resources, marine dialysis, landfilling, and incineration are most common. However, the impact of such waste treatment on the global environment is enormous, and such a global problem may not be possible in Korea since January 2011. There will be no.

In addition, in the case of infectious medical waste discharged from the hospital, sterilization is required, and incineration is the mainstream in an external treatment plant.

Since such incineration carbonizes waste at a high temperature, it is possible to replace the sterilizer and improve the smell so that it can be sanitized. The conventional technique related to this is shown by patent documents 1-4, for example.

1. Japanese Patent Application Publication No. 2006-7111 (pp. 12-25) 2. Japanese Patent Publication No. 2005-207641 (pages 5 to 10, Fig. 1) 3. Japanese Patent Publication No. 2004-238542 (pages 5 to 8, Fig. 1, Fig. 2) 4. Japanese Patent Application Publication No. 2007-203281 (p. 12, Fig. 8, Fig. 9) Although such a prior art is proposed, the technique described in the conventional patent document 1 requires a lot of time for waste treatment by fermentation. In addition, the conventional patent document 2 discloses an apparatus for injecting crushed solids of paper diapers into an incinerator, and incineration thereof, but requires a large amount of fuel consumption, thereby lowering energy efficiency. In addition, the conventional patent document 3 has a problem that the maintenance cost is expensive because it requires a means called a carbonization furnace having a heat generating heater. In addition, most of the medical wastes generated in general medical institutions and nursing homes have been outsourced. Therefore, any of the treatment apparatuses disclosed in the conventional patent documents 1 to 3 is a massive apparatus for handling external consignment, and requires a separate transportation means and a transportation cost in order to transport medical wastes to it. In addition, since the conventional patent document 4 has a structure in which hot air is discharged without a special circulation structure in the carbonization furnace, there is a problem that the thermal efficiency is bad and the discharge temperature of the hot air is considerably high. In addition, the heat conduction efficiency of the carbonized object was low because the temperature difference between the upper and lower portions of the carbonization chamber was caused by the convection phenomenon. In addition, such a conventional technology requires a separate diffuser fan at the bottom in order to circulate high hot air in the upper part, and there is a problem in that thermal efficiency is not economical.

The present invention is to solve the conventional problems as described above, the object of the present invention to solve the problem that has been treated mainly in seawater dialysis, landfilling and incineration, which has not been made so far for organic waste. The present invention provides an indirect heating type carbonization treatment system for wastes and a carbonization vehicle using the same, in which sanitary treatment is sufficiently performed and energy efficiency is improved.

In addition, another object of the present invention is the carbonization treatment of wastes generated in various industries, livestock industry, medical industry, etc., so that carbonization of the wastes is achieved without complete pollution of the surrounding environment. An indirect heating type carbonization treatment system and a carbonization vehicle using the same are provided.

In order to achieve the above object, the present invention, in the carbonization treatment system for carbonizing waste generated in various industries, livestock industry and medical related industry,

A carbonization furnace body, a carbonization chamber embedded in the carbonization furnace body, closed to the outside air, and sealed, and a heat flow passage excluding the front surface where the door portion of the carbonization chamber is formed, wherein the heat flow passage is generated in a burner of the combustion chamber. The hot air is circulated, and a discharge pipe for discharging combustion gas and hot air from the hot flow path is formed.
The carbonization chamber of the carbonization furnace body is formed in a plurality of identical box-type two-chamber structures, each of which is closed and sealed with external air, and has a door for charging and collecting waste on the front surface, and a combustion chamber is formed at the center of the plurality of carbonization chambers. It forms a heat-resistant wall around the circumference, a plurality of inflow pipes from the outlet of the combustion chamber is connected to the lower portion of each carbonization chamber so that hot air is supplied into the heat flow path surrounding the carbonization chamber,
The heat flow path formed around the carbonization chamber is formed in a structure in which hot air is circulated on the upper and lower sides, left and right sides, and the rear side of the carbonization chamber except for the front surface where the hexagonal carbonization chamber door is formed, so that the hot air generated in the combustion chamber is carbonized. After circulating around the entire heat flow path of the carbonization chamber through the inlet pipe of the heat flow path formed on the lower side of the chamber, and is discharged to the stack through the discharge pipe to improve the thermal conductivity efficiency,
The heat flow path has a double wall structure surrounded by the inner wall and the outer wall of the carbonization chamber, and includes a plurality of partition walls that partition the space between the inner wall and the outer wall into a serpentine type structure of the carbonization chamber. Indirect heating type carbonization, which is arranged to surround 5 sides except the door part (waste inlet) so that hot air is discharged after circulating the entire carbonization chamber, thereby improving heat conduction efficiency and suppressing energy consumption. Provide a treatment system.

In order to achieve the above object, the present invention, in a carbonization vehicle equipped with a carbonization treatment system, is provided with a carbonization treatment system which is mounted on the vehicle loading box and movable, wherein the carbonization treatment system includes a carbonization furnace body, and A carbonization chamber built in the carbonization furnace body, and closed with an outside air and having a sealed carbonization chamber, and a heat flow passage excluding the front surface where the door portion of the carbonization chamber is formed, and the hot air flow generated from the burner of the combustion chamber. This circulation provides a carbonization vehicle having a discharge pipe for discharging combustion gas and hot air from the heat flow path.

In order to achieve the above object, the present invention, in a carbonization vehicle equipped with a carbonization treatment system, is provided with a carbonization treatment system installed on the chassis of the trailer towed by the tractor, the carbonization treatment system is movable, the carbonization treatment system is carbonized A furnace chamber, a carbonization chamber embedded in the carbonization furnace body, closed to the outside air, and sealed, and a heat flow passage excluding the front surface where the door portion of the carbonization chamber is formed, wherein the heat flow path is generated from a burner of the combustion chamber. A hot air is circulated, and a carbonization vehicle provided with a discharge pipe for discharging combustion gas and hot air from the hot flow path.

According to the indirect heating type carbonization treatment system of waste according to the present invention and a carbonization vehicle using the same, various wastes generated from sewage pollution, livestock industry, medical relations, elderly nursing homes, etc. in each industry are compacted. On-site treatment can be performed within the site of the generation site to shorten the carbonization time and enable automatic operation.

Further, according to the present invention, the control panel is equipped with an automatic operation program of the burner, so that the working environment for waste disposal can be improved, and an excellent effect that anyone can easily carbonize with a little driving guidance can be obtained. By installing a plurality of box-type carbonization chambers capable of moving differently from the carbonization furnaces, different kinds of wastes can be dispersed in each carbonization chamber, and wastes having different properties and conditions can be carbonized at the same time.

In addition, according to the present invention, a dry gas, which is a kind of energy source, is introduced into a combustion chamber, and excess air is blown into the dry gas to reuse dry gas as hot air, and the carbon chamber is heated by supplying and circulating a heat flow path from the combustion chamber to heat the carbon chamber. As a result, a carbonization treatment facility having excellent energy efficiency can be obtained.

In the present invention, the dry gas from the waste is sent to the combustion chamber in a state in which it is directly mounted on the collecting vehicle, and the inside of the hot flow path is circulated as hot air to implement a method of indirectly heating the plurality of carbonization chambers. The whole carbonization chamber can be heated uniformly, and the wastes put into the carbonization chamber can be completely carbonized.

Therefore, the present invention can immediately carbonize the waste at the place of waste generation, can also be carbonized on the move while recovering the waste, it is also possible to reduce the capacity and weight.

As a result, according to the present invention, the waste can be efficiently recovered, and the waste can be carbonized to be recycled into useful carbides. Thus, not only can the resources be efficiently used, but the environmental pollution caused by the waste can be solved. It has an excellent effect that can be basically solved.

1 is a system configuration diagram showing the indirect heating type carbonization treatment system according to the present invention as a whole.
2 is a front view illustrating a structure in which a plurality of carbonization chambers are formed in a carbonization furnace main body and doors are mounted on the front surface of the carbonization furnace in the indirect heating type carbonization processing system according to the present invention.
Figure 3a is a front view showing a structure in which a plurality of carbonization chamber is formed inside the main body of the carbonization furnace in the indirect heating type carbonization processing system according to the present invention, one door is opened, the other door is closed.
FIG. 3B is a cross-sectional view taken along line AA of FIG. 3A and illustrates a structure in which the door of one carbonization chamber is opened and the door of the other carbonization chamber is closed.
4 is an explanatory view showing a state in which hot air circulates through a carbonization chamber and a surrounding heat flow path provided in an indirect heating type carbonization treatment system according to the present invention.
Figure 5a is a cutaway perspective view showing the internal structure of the heat flow path by cutting the carbonization chamber provided in the indirect heating type carbonization treatment system according to the present invention in the left and right directions.
Figure 5b is a cutaway perspective view showing the internal structure of the heat flow path by cutting the carbonization chamber provided in the indirect heating type carbonization treatment system according to the present invention in the front and rear directions.
6 is an external perspective view showing an example of a carbonization vehicle equipped with an indirect heating type carbonization treatment system according to the present invention.

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

The indirect heating type carbonization treatment system 100 according to the present invention can carbonize waste generated in various industrial, animal husbandry and medical related industries at the place where it is generated, or carbonize during the movement of the vehicle while recovering the waste. In addition, it is a carbonization treatment system composed of a structure of reduced capacity and light weight.

Indirect heating type carbonization treatment system 100 according to the present invention, as shown in Figure 1, as a whole, a carbonization furnace body 110, such a carbonization furnace body 110, the waste is charged in the inside and indirectly The carbonization chambers 120 and 120 'are carbonized, and the carbonization chambers 120 and 120' have a structure in which the doors 122 and 122 'through which waste is charged are formed in front, respectively, to block the interior spaces from the outside air and to seal them.

That is, the carbonization chambers 120 and 120 'are formed in a plurality of box-shaped two-room structure with the same structure inside the carbonization furnace main body 110, as shown in FIGS. 2, 3A, and 3B. For the sake of simplicity, among the plurality of carbonization chambers 120.120 'and related facilities, the same structures and components are given the same reference numerals, and only a subscript (') is additionally identified and identified in the drawings.

Such a carbonization chamber (120, 120 ') forms a space for the waste contained therein, the front is opened, the charging and collection of the waste is made, when closed, the door to block the contact with the outside air ( 122, 122 ') to form a space in which waste is heated.

The carbonization chambers 120 and 120 'are configured such that the front and rear doors 122 and 122' are opened and closed by using a separate conventional hydraulic device (not shown). 120 and 120 'are surrounded by heat flow paths 130 and 130'.

In addition, the carbonization furnace body 110 includes a combustion chamber 140 in which a burner 150 is mounted. The combustion chamber 140 is formed at the center of the plurality of carbonization chambers 120 and 120 '. A heat resistant wall 142 is formed around the plurality of inlet pipes 146 and 146 'from the outlet 144 of the combustion chamber 140 to the lower heat flow paths 130 and 130' of the respective carbonization chambers 120 and 120 '. The hot air is supplied into the heat flow paths 130 and 130 'surrounding the carbonization chambers 120 and 120'.

That is, hot air generated in the burner 150 of the combustion chamber 140 circulates through the heat passages 130 and 130 'provided in the respective carbonization chambers 120 and 120', and combustion gas is discharged from the heat passages 130 and 130 '. And discharge pipes 138 and 138 'for discharging hot air are formed at the exits of the heat flow paths 130 and 130' of the carbonization chambers 120 and 120 ', and are discharged to the stacks 139 and 139'.

The indirect heating type carbonization treatment system 100 according to the present invention uses a refractory material, for example, a refractory brick, in the lower portion of the plurality of carbonization chambers 120 and 120 'of the carbonization furnace body 110, and the heat insulation wall 142. ) Is provided with a combustion chamber 140, and the combustion chamber 140 is equipped with a burner 150 that is heated using LP gas and dry gas discharged from the waste, and supplies hot air to the heat flow paths 130 and 130 '. Indirectly heating the carbonization chamber (120, 120 ') by supplying.

In addition, the indirect heating type carbonization processing system 100 of the present invention is loaded on the vehicle 200, as described later, for example, mounted on a loading box of a truck and movable, or in a chassis of a trailer. It is equipped with a structure that can be towed and moved by a tractor, so that the vehicle can be moved to the site of waste generation to carbonize the waste immediately, and recycling can be carried out to reduce environmental load.

In addition, the combustion chamber 140 of the indirect heating type carbonization processing system 100 of the present invention includes a burner 150 using LP gas fuel and dry gas as fuel, and the burner 150 includes an LP gas tank ( An LP gas pipe 154 to which LP fuel is supplied from 152 is connected.

In addition, the burner 150 is connected to the carbonization chambers 120 and 120 'of the carbonization furnace body 110 and is provided with dry gas supply pipes 156 and 156' provided with dry gas, and connected to a blower 160 and 160 'for combustion. Combustion air pipes 162 and 162 'into which air is introduced are connected to inject the flame of the burner 150 into the combustion chamber 140, and mix with air sent from the blowers 160 and 160' to generate combustion hot air, and the combustion chamber 140 It is to supply hot air to the heat flow path (130,130 ') through.

In the combustion system structure of the burner 150 as described above, the combustion air pipes 164 and 164 'of the blowers 160 and 160' are connected to the dry gas transfer pipes 156 and 156 'so as to supply dry gas to the burner 150. Will be provided.

To this end, the combustion air supporting pipes 164 and 164 'are equipped with automatic opening and closing valves 164a and 164a' and opened and closed. When the automatic opening and closing valves 164a and 164a 'are opened, the dry gas transfer pipes 156 and 156' are opened. By supplying the conveyed air through this, dry gas generated in the carbonization chambers 120 and 120 'is supplied to the burner 150 to be used for combustion.

The burner 150 of the combustion chamber 140 as described above is controlled through the touch panel display 172 of the control panel 170 independently disposed outside the carbonization furnace body 110, as shown in FIG. Temperature management of the carbonization chambers 120, 120 ′ is performed by the temperature sensor 174, preferably UV (Ultraviolet) sensor, mounted in the combustion chamber 140 in real time on the control panel 170 via the burner control unit 176. Is sent and the temperature is output to the outside.

As such, the combustion output of the burner 150 using LP gas fuel and dry gas of the carbonization chambers 120 and 120 'is 40,000 kcl / h to 460,000 kcl / h, and each carbonization chamber 120 and 120 is used. ') Is heated to a temperature of 0 ℃ ~ 1000 ℃ so that the waste inside the carbonization chamber (120 120) is carbonized by high heat without direct oxidation.

That is, the carbonization chambers 120 and 120 'are sealed and shielded from the outside and are oxygen free, so when the waste is heated at a high temperature, the waste is carbonized instead of directly burned.

The carbonization treatment thus suppresses the combustion of wastes, thus suppressing the generation of harmful substances. In addition, carbon dioxide is not emitted to the atmosphere, and no thyxin is generated, and the environmental load polluting the surrounding environment is extremely low.

In addition, carbides generated after carbonization of wastes become raw materials for recycling such as fossil fuel substitutes, and volume reduction of wastes is possible, and LP gas fuel is saved by using dry gas from wastes as the main raw material. Saving is made.

Meanwhile, in the indirect heating type carbonization processing system 100 of the present invention, as shown in FIG. 4, the heat flow paths 130 and 130 'formed around the carbonization chambers 120 and 120' are hexagonal carbonization chambers 120 and 120 '. Upper and lower surfaces of the carbonization chambers 120 and 120 'except for the front surface where the doors 122 and 122' are formed, and the combustion chamber 140 is formed in a serpentine type structure having a flow path through which hot air circulates on the left and right sides and the rear surface. The hot air generated in circulates around the carbonization chambers 120 and 120 'through the inlet pipes 146 and 146' and is discharged to the outside through the discharge pipes 138 and 138 '.

That is, the heat flow paths 130 and 130 'have a double wall structure surrounded by inner walls 124 and 124' and outer walls 126 and 126 'of the carbonization chambers 120 and 120', as shown in FIGS. 5A and 5B. A partition is formed by providing a plurality of partitions 128 and 128 'that divide the space between the inner wall 124 and 124' and the outer wall 126 and 126 'into a serpentine type structure.

The heat flow paths 130 and 130 'are arranged to surround the five surfaces except for the door portion (waste inlet) of the carbonization chambers 120 and 120', and are discharged after the hot air circulates through the entire carbonization chambers 120 and 120 '. By having such a structure, the thermal conductivity of the carbonization chambers 120 and 120 'is increased and energy consumption is greatly suppressed.

As described above, the hexagonal carbonization chambers 120 and 120 'have been described as a double wall structure in which five surfaces except the front surface are surrounded by heat flow paths 130 and 130' made of a serpentine type, but the present invention is limited thereto. Heat conduction efficiency by arranging the heat flow paths 130 and 130 'provided in the carbonization chambers 120 and 120' on five sides by using a sand pipe (not shown) to circulate the hot air. At the same time, the energy consumption may include all other structures that are suppressed.

Meanwhile, the heat flow paths 130 and 130 'formed around the carbonization chambers 120 and 120' may be used as a cooling channel structure for cooling the carbonization chambers 120 and 120 'after the carbonization of the waste. The combustion state of 150 is stopped and the cold air provided from the blowers 160 and 160 'is supplied to the heat flow paths 130 and 130' while the hot air is discharged.

Therefore, during the cooling process after the carbonization treatment, forced air cooling can be obtained by sending cooling blowers of the blowers 160 and 160 'through the heat flow paths 130 and 130', and the carbonization time is improved through the forced cooling. And the cooling time can be shortened.

The indirect heating type carbonization processing system 100 according to the present invention configured as described above may be mounted on the carbonization vehicle 200 as shown in FIG. 6.

That is, it is mounted on a vehicle loading box and movable, or is installed on a chassis of the trailer towed by the tractor (moving) is made of a structure that is movable.

As described above, the indirect heating type carbonization processing system 100 according to the present invention includes a plurality of the carbonized furnace main body 110 and the carbonized furnace main body 110, which are blocked by outside air and sealed. The heat passages 130 and 130 'surrounding the five surfaces except for the front side in which the carbonization chambers 120 and 120' and the doors 122 and 122 'of the plurality of carbonization chambers 120 and 120' are formed. And circulates hot air generated in the burner 150 of the combustion chamber 140, and discharges combustion gas and hot air from the hot flow paths 130 and 130 'to the outside through discharge pipes 138 and 138'. It can be.

Reference numerals 180 and 180 'are carbonization chamber control units embedded in the control panel 170, (V) is an open / close valve, (T) is a thermocouple for detecting carbonization chamber temperature, and 210 is a vehicle 200. It is a generator mounted on.

In the carbonization vehicle 200 equipped with the indirect heating type carbonization treatment system 100 of the present invention as described above, a driver or an operator traverses a waste generating place using a vehicle.

At this time, the driver or worker starts by loading some bins 220 into the carbonization vehicle 200. And collect the collection box 220 containing the waste to go to the waste discharge. The collection box 220 may be made of, for example, a reticulated container box, but the present invention is not limited thereto.

And the driver provides an empty collection box 220 instead of receiving the collection box 220 containing the waste from the waste discharge.

When the waste is collected as described above, the waste is collected in a collection box 220 in a site of various industrial, livestock, or medical institutions where waste is discharged, and the plurality of carbonization chambers 120, 120 'or any one of them. After charging to 120, 120 ', the burner 150 of the combustion chamber 140 can be immediately carbonized in the field.

In this case, the driver operates the control panel 170 mounted on the vehicle 200. The control panel 170 is equipped with various switches (not shown) to automatically ignite the burner 150, and initially Burner 150 is burned using LP gas fuel.

When the burner 150 is burned to generate hot air in the combustion chamber 140 to carbonize waste in the carbonization chambers 120 and 120 ', dry gas is generated in the carbonization chambers 120 and 120'.

At this time, when the automatic shut-off valves 164a and 164a 'mounted on the combustion air pipes 164 and 164' are opened, dry gas is supplied to the burner 150, and the burner 150 is combusted using the supplied dry gas. In this case, the LP gas fuel may be blocked to burn the burner 150 only with dry gas.

However, when the dry gas is insufficient, the temperature of the combustion chamber 140 may be lowered. At this time, the LP gas fuel is supplied again to further burn the burner 150 to add heat.

At this time, the temperature of the combustion chamber 140 is detected using a temperature sensor 174, preferably a UV (Ultraviolet) sensor, and based on the detected temperature, the control panel 170 may be a dry gas or LP gas fuel. By adjusting the flow automatically, the combustion chamber is heated to 40,000 kcl / h to 460,000 kcl / h, and each carbonization chamber 120 and 120 'is heated to a temperature of 0 ° C to 1000 ° C. Therefore, the waste can be carbonized immediately at the work site where the waste is collected.

In this case, at a time when a predetermined amount of waste is collected, the driver may operate a separate compressor (not shown) mounted on the carbonization vehicle 200, and charge the waste in the compressed state into the carbonization chambers 120 and 120 ′. It can also be carbonized.

As described above, the present invention collects wastes and carbonizes them immediately in the vehicle 200, thereby preventing food decay and contamination, which are frequently generated in summer, and collecting parasitic germs at the same time. Can be sterilized.

Alternatively, the present invention loads the driver collection box 220 in the installation space of the vehicle, so that the waste is carbonized through the carbonization process as described above in the carbonization chamber (120,120 ') while moving to the next waste discharge destination. can do.

Then, when the next waste discharge destination is reached, the collection bin 220 containing the waste and the like is collected and the empty collection bin 220 loaded is exchanged and provided.

At this time, the collected waste is charged into the carbonization chamber 120, 120 'or the empty carbonization chamber 120, 120' which is similarly carbonized, and then carbonized immediately at the waste discharger, or when the carbonization work is ready, It can also be carbonized while traveling while moving to the discharge destination.

In this way, the carbonization of most of the waste is completed by the time the carbonization vehicle returns to the business place of the starting point after the circulation of the discharge destination is finished, and the carbonization system 100 is stopped after the arrival of the business.

In this case, the carbonization system 100 is still in a high temperature state.

However, if necessary, the driver may stop the burner 150 combustion state of the combustion chamber 140 and supply the cold air provided from the blowers 160 and 160 'to the heat flow paths 130 and 130' in a state where the hot air is discharged.

That is, by simply sending the cooling air of the blowers 160 and 160 'to the heat flow paths 130 and 130' while the burner 150 is stopped, the forced air cooling function can be obtained, and the carbonization chambers 120 and 120 'are provided. The cooling time can be forcibly shortened.

As described above, the carbonization vehicle according to the present invention is very efficient because it can carbonize the waste while traveling while collecting waste while traversing the waste discharge destination such as various industrial sites, livestock industries or medical institutions.

In particular, since waste discharge points such as convenience stores and hospitals are mostly dotted, carbonization can be performed by utilizing the time traveled while driving.

In addition, food waste and the like are carbonized at the same time of collection, and thus, it is possible to prevent the spread of contamination caused by food decay and propagation of germs, and also to sterilize an infectious waste generated in a medical institution.

In addition, useful carbides can be produced from the waste, and thus the waste can be recycled or reused.

In addition, since the empty bin 220 that has been treated can be provided as an exchange bin 220 for the next waste discharge, carbonizing the minimum bin 220 without carrying many bins 220. It is enough to put on the processing vehicle 200, it is possible to maximize the space efficiency.

In addition, carbonization reduces the volume of waste by about 1/25, thus eliminating the need for trucks to frequently reciprocate between waste sources and waste treatment plants, as is conventional, resulting in very economical and high collection efficiency.

In addition, since the dry gas generated from the waste itself generated during the carbonization of the waste is used as a heat source, fuel can be reduced and more efficient.

As described above, the carbonization vehicle equipped with the indirect heating type carbonization processing system 100 according to the present invention may be left as it is when the carbonization of waste is completed by the time the work is completed and returned to the office.

In addition, it is possible to save time because it does not need to take out the collected waste and incineration separately as in the prior art, and as a result, it is possible to concentrate on waste collection work all day.

In addition, there is no waste end that becomes difficult to dispose of waste due to the wastes left unattended as in the prior art, and when the carbonized vehicle is left for a certain time and naturally cooled, the doors 122 and 122 'of the carbonization chambers 120 and 120' are opened and carbides are removed. I can easily take it out.

As mentioned above, although this invention was demonstrated and demonstrated with reference to the specific preferable Example, etc., this invention is not limited to the said Example, The technique which the said invention belongs to in the range which does not deviate from the technical idea of this invention. It is obvious that various changes and improvements can be made by those skilled in the art.

Therefore, it will be apparent to those skilled in the art that the structure of the carbonization apparatus shown in the drawings may be simply changed and improved without departing from the spirit and scope of the present invention. However, the present invention includes all such simple modified and improved structures. It is.

100 ...... Indirect Heating Carbonization System 110 ...... Carbon Furnace Body
120,120 '...... Carbon 122.122' ..... Door
124,124 '..... inner wall 126,126' ..... outer wall
128,128 '...... Bulkhead 130,130' .... Heat Euro
138,138 '...... outlet 139,139' ...... mute
140 ...... Combustion chamber 142 ...... Heat-resistant wall
144 ...... Outlet 146,146 '...... Inlet pipe
150 ...... Burner 152 ...... LP Gas Tank
154 ...... LP gas pipe 156,156 '...... Dry gas transfer pipe
160,160 '..... Blower 162,162' ...... Combustion air pipe
164,164 '..... Combustion air branch 164a, 164a' ...... Automatic shut-off valve
170 ...... Control panel 172 ...... Touch panel display
174 ...... temperature sensor 176 ...... burner control unit
180,180 '...... Carbon Chamber Control Unit 200 ...... Carburized Vehicle
210 ...... Generator 220 ...... Collector
T ............ Thermocouple V ...... Valve

Claims (10)

In the carbonization treatment system for carbonizing waste generated in various industries, animal husbandry and medical industry,
The carbonization furnace body 110, the carbonization chambers 120 and 120 ′ embedded in the carbonization furnace body 110 and blocked by outside air, and the doors 122 and 122 ′ of the carbonization chambers 120 and 120 ′ are formed. It has a heat flow path (130,130 ') excluding the front, hot air generated in the burner 150 of the combustion chamber 140 is circulated through the heat flow path (130, 130'), the heat flow path (130, 130 ') Discharge pipes 138 and 138 'are formed to discharge combustion gas and hot air from the
The carbonization chambers 120 and 120 'of the carbonization furnace body 110 are closed and sealed with external air, and are formed in a plurality of identical box-type two-room structures in which doors 122 and 122', on which a charge and collection of waste are formed, are formed on the front surface, respectively. The combustion chamber 140 is formed at the center lower portion of the plurality of carbonization chambers 120 and 120 ', and forms a heat resistant wall 142 around the plurality of inflow pipes 146 and 146' from the outlet 144 of the combustion chamber 140. ) Is connected to the lower side of each carbonization chamber (120,120 ') so that hot air is supplied into the heat flow path (130,130') surrounding the carbonization chamber (120,120 '),
The heat flow paths 130 and 130 'formed around the carbonization chambers 120 and 120' have hot air circulated on the upper and lower sides, left and right sides, and the rear side of the carbonization chambers 120 and 120 'except for the front surface where the hexagonal carbonization doors 122 and 122' are formed. Hot air generated in the combustion chamber 140 through the inlet pipes 146 and 146 'of the heat flow paths 130 and 130' formed at the lower sides of the carbonization chambers 120 and 120 '. After circulating around the entire heat flow path (130,130 ') of the discharge through the discharge pipe (138,138') to the stack (139,139 ') is configured to improve the thermal conductivity efficiency,
The heat flow paths 130 and 130 'have a double wall structure surrounded by inner walls 124 and 124' and outer walls 126 and 126 'of the carbonization chamber 120 and 120', and are arranged between the inner walls 124 and 124 'and the outer walls 126 and 126'. It is equipped with a plurality of partitions 128 and 128 'partitioning the space into a serpentine type structure and is arranged to surround five sides except for the door portion (waste inlet) of the carbonization chamber 120 and 120'. Indirect heating type carbonization processing system 100, characterized in that the hot air is discharged after circulating through the entire carbonization chamber (120,120 '), the heat conduction efficiency is increased and energy consumption is suppressed. The combustion chamber 140 of the carbonization furnace body 110 includes a burner 150 for fueling the LP gas fuel and the dry gas through the dry gas transfer pipes 156 and 156 '. Inject the flame of the burner (150) burned in 140, and indirect heating type carbonization processing system 100, characterized in that it is mixed with the air sent from the blower (160,160 ') to generate a combustion hot air. The burner 150 of the combustion chamber 140 is connected to the LP gas pipe 154 to which the LP gas fuel used as the main fuel is supplied, and the carbonization chambers 120 and 120 of the main body of the carbonization chambers 120 and 120 '. 'Is connected to the dry gas supply pipe (156,156') is provided with a dry gas is connected, the combustion air pipes (162, 162 ') is connected to the blower (160, 160') flows the combustion air, the blowers (160, 160) ') Combustion air branch pipes (164, 164') is connected to the dry gas transfer pipes (156, 156 ') indirect heating type carbonization treatment system 100, characterized in that to provide a transfer air for supplying dry gas to the burner 150 ). delete The burner 150 of the combustion chamber 140 is controlled through the touch panel display 172 of the control panel 170 independently disposed outside the main body of the carbonization chambers 120 and 120 '. The temperature management of the 120 and 120 'is performed by sending information from the temperature sensor 174 mounted in the combustion chamber 140 to the control panel 170 in real time so that the temperature is output to the outside, and the combustion output of the burner 150 is 40,000 kcl. / h ~ 460,000kcl / h, the indirect heating type carbonization treatment system 100, characterized in that the carbonization chamber (120, 120 ') can be adjusted to a temperature of 0 ℃ ~ 1000 ℃. delete delete The heat flow paths 130 and 130 'formed around the carbonization chambers 120 and 120' allow cooling of the carbonization chambers 120 and 120 'by passing cold air provided from the blowers 160 and 160' after carbonization of the waste. Indirect heating type carbonization treatment system 100, characterized in that also serves as a structure of the cooling passage. A carbonization vehicle (200) comprising the carbonization treatment system (100) according to claim 1. delete

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