KR101072009B1 - Cremation furnaces system reformed structure of clearing pollution material - Google Patents

Abstract

The present invention relates to a cremation system with a contaminant gas removal structure. The present invention relates to a contaminant removal means formed in a multi-stage manner in order to minimize the emission of contaminants. It is an object of the present invention to provide a cremation system in which a contaminant gas removal structure is reinforced so as to organically connect and control each device, and to create an optimum removal environment through programmed control data for each device.

Application of the present invention, by controlling the fuel injection amount and the combustion air injection amount as a whole according to the temperature and pressure of the main combustion furnace and the reburn furnace, to induce complete combustion in the furnace and to control the combustion gas to maintain the proper temperature, 1, 2 It is effective to remove contaminants by connecting the tea bag filter and catalytic reactor in a multi-stage direct connection method, so that effective contaminants can be removed by each component, and each device is organically linked and controlled to achieve optimal combustion. In addition to being able to induce, there is an advantage that it is possible to complete the removal of contaminants.

Pollutant gases, white lead, nitrogen oxides, crematoriums, crematoriums.

Description

CRYSATION FURNACES SYSTEM REFORMED STRUCTURE OF CLEARING POLLUTION MATERIAL}

The present invention relates to a cremation system with a contaminant gas removal structure, and more particularly, to construct a contaminant removal means made of a multi-stage method in order to suppress the discharge of contaminants in detail, and to discharge the contaminant in a completely removed state. The present invention relates to a refurbishment system reinforced with a contaminant gas removal structure that allows each device to be organically linked to control and to create an optimum removal environment through programmed control data for each device.

As is well known, the conventional crematorium system cremates a corpse to make it into the ashes, and then pulverizes the ashes in the bone chamber to collect the ashes in a powdered state. Equipped with a system to

More specifically, the cremation culture, which has recently been increasing preferably, can enhance the efficient use of narrow lands, prevent the spread of hate facilities such as graveyards, and settle the culture rapidly in recent years in order to promote a sound park culture. There is a situation.

In other words, through the ossuary system at the end of the cremation culture, it is intended to move away from the existing Confucian culture and burial place culture, and to enter a more advanced and advanced funeral culture.

However, in order to revitalize the ossuary system and improve the efficiency of the land, it is necessary to establish a sound perspective on the crematory system, and the technical development and advancement of the crematory system are the most important to solve the negative view of the general public.

In other words, the conventional crematory system has a large technical problem that the pollutants are actually being discharged into the atmosphere rather than psychologically negative as the place where the makeup is made because nitrogen oxides are contained in the combustion material of the toilet. It was a problem, and since white smoke was released in the year of cremation, white smoke was psychologically placed as a factor that gave a negative view of the construction of the crematory.

The present invention has been made in view of the above-described state of the art, and in order to minimize the emission of contaminants, the contaminant removal means made of a multi-stage method is constructed, and each apparatus is discharged in a state in which the contaminants are completely removed. It is an object of the present invention to provide a refurbished system reinforced with a contaminant gas removal structure for organically linked control and to create an optimum removal environment through programmed control data for each device.

In order to achieve the above object, according to a preferred embodiment of the present invention has a crematory compartment divided into a main combustion furnace and a reburn furnace, and a trolley access control means having a thermal insulation door that is automatically opened and closed with an in-vehicle trolley transfer unit therein. And a cremation system in communication with the reburn furnace of the cremator and exhausting the combustion gas with the final stack, wherein the flue gas and the communicating tube are connected to the reburn furnace, and a cooling gas is circulated therein to reduce the temperature of the exhaust gas. Temperature control means comprising a gas heat exchanger for lowering the temperature to a set temperature, and a temperature sensing unit for sensing a temperature of the exhaust gas; It is installed between the communication pipe and the gas heat exchanger to the reburn furnace, and installed at the front of the contaminant removal means and the gas heat exchanger and the chimney, respectively, and a blower for attracting the exhaust gas, and a pressure sensing unit for detecting the pressure of the reburn furnace and each communication tube. And a blowing control means including a pressure control unit for controlling the blower at a predetermined pressure; A primary bag filter which firstly processes the exhaust gas transferred and communicated with the heat exchanger, a bag filter which is in communication with the first bag filter and secondaryly processes the exhaust gas, and a bag filter which is in communication with the secondary bag filter A catalytic reactor for tertiary treatment is connected in multiple stages to remove contaminants including nitrogen oxide, dioxin and white smoke due to combustion; Polluting gas, characterized in that it comprises a cosmetic treatment control means for controlling the temperature, pressure, exhaust gas amount to a predetermined value in association with the devices of each means, and controlling the processing speed of the pollutant removal means according to the exhaust gas amount There is provided a cremation system with a reinforced structure.

Preferably, the gas heat exchanger is configured in connection with a heat exchanger damper control unit for controlling the injection amount of the cooling gas according to the temperature and the heat exchanger blower is controlled by the heat exchanger damper control unit for controlling the blowing amount of the cooling air. Provided is a cremation system reinforced with a contaminant gas removal structure.

Preferably, the gas heat exchanger is a primary and secondary gas heat exchanger for lowering the combustion gas blown from the reburn furnace at least 850 ℃ to 400 ℃; It consists of a tertiary gas heat exchanger that drops the combustion gas dropped to 400 ° C. to 250 ° C. to 300 ° C., and the first and second gas heat exchangers have no air dilution, thereby suppressing dioxin resynthesis. Provided is a cremation system with a contaminant gas removal structure that is configured to suppress white smoke through a temperature drop.

Preferably, the tertiary gas heat exchanger and the heat exchange in the rear end of the communication pipe for communicating the cooling gas heated up to the stack; Provided is a cremation system provided with a predetermined portion of the communication tube, and further comprising a regeneration heat recovery device for recovering regeneration heat.

Preferably, the temperature control means is installed in at least two or more to the crematory system through a branched communication pipe is installed in the crematory system with a contaminated gas removal structure, characterized in that installed to utilize the heat of the appropriate temperature as renewable energy Is provided.

Preferably, the secondary filter dust collector is provided with a branch pipe in the upper portion, and the secondary slaked lime / activated carbon supply unit for supplying the hydrated lime and activated carbon to the branch pipe is combined, the activated carbon and the slaked lime is installed to be introduced into the branch pipe Provided is a cremation system with a contaminant gas removal structure.

Preferably, the primary filter dust collector is further provided with a first calcined lime / activated carbon supply unit for recycling the slaked lime and activated carbon filled into the inside of the second filter dust collector to the primary bag filter at its front end. Provided is a cremation system with a contaminant gas removal structure.

Preferably, the primary and secondary filter dust collector is connected to the compressed air for compressing air, the air storage tank for storing the compressed air, and the air dryer for removing moisture contained in the compressed air stored in connection with the air storage tank It is provided with a cremation system reinforced with a contaminant gas removal structure, characterized in that configured to receive compressed air.

Preferably, the lower end of the first and second filter dust collector is further provided with a fly ash processing unit for processing fly ash, discharged to the outside of the condensation gas removal structure reinforcement structure, characterized in that the compressed treatment A system is provided.

Preferably, the catalytic reactor further comprises an ammonia tank for storing ammonia and a circulation pump for supplying ammonia from the ammonia tank to reduce nitrogen oxide and white lead through hydrolysis of ammonia. There is provided a cremation system with a degassing structure.

Preferably, the cosmetic treatment control means comprises a communication module which is in communication with each device of the vehicle access control means, the blowing control means, the temperature control means, the pollutant removal means; A data storage unit for storing control data for each device and sequential control data according to sensed values; A key input unit for generating a manual input value for the control signal; Provided is a cremation system with a contaminant gas removal structure that is configured to include a monitor that displays the driving status of each device.

Preferably, it is configured for each location so as to monitor the state of the front room hall, the machine room and the bone chamber, the stack of the crematory, and further comprising a CCTV camera for transmitting the image data to the cosmetic treatment control means Provided is a cremation system with a contaminant gas removal structure.

The refurbishment system with the contaminant gas removal structure according to the present invention controls the fuel injection amount and the combustion air injection amount as a whole according to the temperature and pressure of the main combustion furnace and the reburn furnace, thereby inducing the complete combustion in the furnace and the combustion gas to obtain the proper temperature. It is controlled to maintain, and it is effective to remove pollutants completely by connecting the first and second bag filter with the catalytic reactor in a multi-stage direct connection method, so that effective pollutants can be removed by each component. It can be linked and controlled to achieve optimal burnout and at the same time, complete removal of contaminants.

EMBODIMENT OF THE INVENTION Hereinafter, this invention is demonstrated in detail with reference to drawings.

1 is a side view of a cremator showing a state in which a crematory system with a contaminated gas removal structure is constructed according to an embodiment of the present invention, and FIG. 2 is a cremation reinforced with a contaminant gas removal structure according to an embodiment of the present invention. This is a block diagram showing the system.

Referring to this, the furnace system reinforced with a contaminant gas removal structure according to an embodiment of the present invention is to construct a contaminant removal means made of a multi-stage method in order to suppress the emission of contaminants, and the contaminants are completely removed. It is a system that makes it possible to organically connect and control each device so as to be discharged from the state, and to create an optimal removal environment through the associated control data of each programmed device.

More specifically, the contaminant gas system 2 with the contaminant gas removal structure according to an embodiment of the present invention has a structure of a basic cosmetic bar, and the structure of the basic cosmetic furnace 4 is a main combustion furnace 8. And the reburn furnace 12 are partitioned and formed in a stacked state, and the main combustion furnace 8 and the reburn furnace 12 are equipped with a main combustion burner 10 and a reburn burner 14, respectively. That is, the crematorium 4 is configured to completely burn the dead body and the combustion gas for burning the dead body through a plurality of combustion furnaces, so as to minimize the discharge of pollutants, and is included in the system of the present invention. The cosmetic treatment control means 70 automatically controls the fuel supply and the oxygen supply to the main combustion furnace 8 and the reburn furnace 12 installed in the cosmetic furnace 4 so that complete combustion is achieved.

In addition, the front of the crematory (2) is provided with a tube, or the front chamber 6 for cooling the furnace bogie (not shown) is provided, the communication tube 18 is provided at the upper end of the front chamber (6) It is connected to join with the communication tube of the reburn chamber (16).

In addition, the toilet 2 is provided with a heat insulating door 22 that is automatically opened and closed between the front chamber 6, the lower part of the toilet 2, a roller device (not shown), chain, chain It consists of a gear is built in the furnace bogie transfer unit 20 for automatically transferring the bogie bogie to the center position of the crematorium (2).

In particular, the cremation system (2) with a contaminated gas removal structure according to an embodiment of the present invention is provided with a temperature control means 32 for adjusting the temperature of the combustion gas to a usable temperature, the temperature control The means 32 is connected to the flue of the reburn furnace 12 and the communication tube 16, and the gas heat exchanger (37, 38) to flow the cooling gas therein to lower the temperature of the combustion gas to a predetermined temperature: , The first and second gas heat exchanger), and the temperature sensing unit 34 for sensing the temperature of the combustion gas.

At this time, the combustion gas discharged from the reburn furnace 12 is a high temperature whose temperature reaches 850 ℃ or more, while activating the internal material of the contaminant removing means 43 configured in the subsequent stage by using the heat of the combustion gas. In order to improve the durability of the communication pipe and each device, quenching is preferably performed at about 400 ° C to 250 ° C. The primary and secondary gas heat exchangers (37, 38) provided in the present invention is provided with a blower (26) for the transfer of combustion gas at its front end, when the combustion gas is circulated as a plate-type convection heat exchanger, Cooling is rapidly cooled by the cooling air blown in contact with the primary and secondary gas heat exchangers 37 and 38, thereby effectively reducing the temperature.

In more detail, the primary and secondary gas heat exchangers 37 and 38 are indirect heat exchange methods in which a plurality of heat transfer plates (not shown) are provided and indirect heat exchange is performed by circulating combustion gas and cooling air therebetween. , The heat exchanger is made of a special shape bending to increase the contact surface through the heat transfer plate of the embossed shape, to prevent thermal expansion, the primary and secondary gas heat exchanger (37, 38) is a laminated structure, respectively, combustion air Is first lowered to a predetermined temperature while passing through the primary gas heat exchanger (37), and then to the final set temperature while passing through the secondary gas heat exchanger (38).

In particular, the primary and secondary gas heat exchangers (37, 38) is further provided with a heat exchange damper control unit 36 for adjusting the injection amount of the cooling gas in accordance with the temperature, the cosmetic treatment control means 70 is Detects the temperature of the combustion gas flowing into the first and second gas heat exchangers (37, 38) and generates a control signal to the heat exchange damper control unit 36 according to the temperature to control the injection amount of cooling air to contaminate The removal means 43 allows the combustion gas at an optimum preset temperature (eg, about 400 ° C.) to flow.

More specifically, the first and second gas heat exchangers for lowering the combustion gas blown from the reburn furnace 12 and higher than 850 ℃ to 400 ℃; It consists of a tertiary gas heat exchanger that drops the combustion gas dropped to 400 ° C. to 250 ° C. to 300 ° C., and the first and second gas heat exchangers have no air dilution, thereby suppressing dioxin resynthesis. It is the structure that suppresses or removes white lead through temperature drop.

At this time, by generating a control signal to the heat exchange damper control unit 36 to adjust the injection amount of the cooling air, more specifically, the heat exchange damper control unit 36 is the cooling air to the primary and secondary gas heat exchanger ( By controlling the driving of the heat exchanger blower 35 in conjunction with the heat exchanger blower 35 for blowing to 37, 38, the amount of cooling air is adjusted.

Preferably, the temperature adjusting means 32 may be installed so that at least two or more are installed in the entire system of the cremator so as to utilize heat of a proper temperature as a renewable energy through a branched communication tube.

On the other hand, in the cremation system (2) of the contaminated gas removal structure according to an embodiment of the present invention is installed at the rear end of the communication tube 16 and the front of the stack 60 of the reburn furnace 12 to attract the exhaust gas. A blower 26 and a heat exchanger blower 35 provided at the front end of the primary and secondary gas heat exchangers 37 and 38 to blow cooling gas, and the reburn furnace 12 and each communication tube 16 are provided. And a blowing control means (24) comprising a pressure detecting part (28) for detecting the pressure of the pressures (40, 42, 58) and a pressure control part (30) for controlling the blower at a predetermined pressure. (24) maintains the pressure inside the furnace due to the discharge pressure of the combustion gas, and by appropriately adjusting the discharge pressure to achieve a complete combustion of the toilet 4, and effectively remove the contaminants contained in the combustion gas Make it possible. The blowing control for each device of the blow adjusting means 24 is also controlled automatically by the cosmetic treatment control means 70 by detecting the pressure applied to each communicating tube, and the control value of the blower 26 according to the pressure for each position in advance. The cosmetic treatment control means 70 is programmed.

At this time, since the cooling air passing through the first and second gas heat exchangers 37 and 38 is heated to high temperature air at the time of heat exchange, the first and second gas are used to preheat the catalytic reactor 55 with the elevated air. The communication tube 42 which distributes the cooling air to the heat exchangers 37 and 38 is a tube which is connected to the tertiary heat exchanger 39 and distributes the heated air to the tertiary heat exchanger 39.

That is, the tertiary heat exchanger (39) is provided at the front end of the catalytic reactor (55), and is different from the pipe for circulating the combustion gas, the circulation pipe (42) through which the heated cooling gas (about 400 ° C) is circulated. It is a heat exchanger to receive the gas heated up through the preheated combustion gas at a preheating temperature of 250 ℃ to 300 ℃.

That is, the catalytic reactor 55 is the optimum nitrogen oxide and dioxin removal efficiency at a preheating temperature of 250 ℃ to 300 ℃, the temperature of the catalytic reactor 55 through the third heat exchanger 39 is Allow to preheat to a temperature of 250 ° C to 300 ° C.

In addition, in the cremation system (2) of the contaminant gas removal structure is reinforced according to an embodiment of the present invention 1 for primary treatment of the exhaust gas communicated with the primary and secondary gas heat exchangers (37,38). A tea bag filter 44; A secondary bag filter 48 in communication with the bag filter 44 for secondary treatment of exhaust gas; The catalytic reactor 55 communicating with the secondary filter dust collector 48 and tertiaryly treating the exhaust gas is connected in multiple stages to remove contaminants including nitrogen oxide, dioxin, and white smoke due to combustion. ) Is provided.

The primary filter dust collector 44 and the secondary filter dust collector 48 is a tank (not shown) for storing powder-type slaked lime, an activated carbon storage tank (not shown) for storing activated carbon, and a transfer pump 1 , Secondary slaked lime / activated carbon supply unit (51,52) bar, slaked lime pretreatment coating function to remove secondary acid gas, dioxin, etc., and activated carbon to remove fine dust and dioxin, HCl, SOx contaminants Remove

On the other hand, a secondary slaked lime / activated carbon supply unit 52 for supplying hydrated lime and activated carbon to the upper portion of the secondary filter dust collector 48 is in communication with, the front of the primary filter dust collector 44, the secondary filter dust collector The primary slaked lime / activated carbon supply part 51 which recycles the hydrated lime and activated carbon discharged | emitted to the discharge stage of 48 with the primary bag filter 44 is connected.

That is, activated carbon absorbs dioxins or heavy metals on the surface of the activated carbon, and is introduced into the first and second bag filters 44 and 48 to secondaryly remove contaminants collected in the activated carbon in a bag filter manner.

In addition, the primary and secondary filter dust collector (44, 48) is an air compression unit for compressing air, an air storage tank for storing the compressed air, and removes the moisture contained in the compressed air stored in connection with the air storage tank Compressed air supply unit 50 is configured to be connected to the air dryer is configured to receive the compressed air, the high-efficiency filter cloth (P-48 material) is built in the primary and secondary bag filter 44,48 Compressed air is allowed to pass through the activated carbon and filter cloth provided in the primary and secondary bag filters 44 and 48 by using the compressed air of the compressed air supply unit 50.

In addition, in the cremation system 2 having the contaminated gas removal structure according to an embodiment of the present invention, a fly ash processing unit 54 for processing fly ash at the lower ends of the first and second bag filters 44 and 48 is further provided. It is provided to discharge the collected fly ash to the outside to be compressed.

On the other hand, the catalytic reactor 55 provided in the refurbishment system 2 with the contaminant gas removal structure according to an embodiment of the present invention is an ammonia tank (not shown) for storing ammonia, and the ammonia from the ammonia tank A circulation pump (not shown) for supplying the ammonia supply unit 56 is further provided to reduce the nitrogen oxide through a hydrolysis method of ammonia.

The front end of the catalytic reactor 55 is provided with a tertiary heat exchanger (39) to match the optimum temperature conditions in which the catalyst is activated in the catalytic reactor (55), thereby suppressing the generation of white smoke as a separate white smoke removal device Is unnecessary.

In addition, the tertiary gas heat exchanger (39) is connected to a communication tube (57) which communicates the cooling gas heated by heat exchange at the rear end thereof with a stack, and is provided in a predetermined portion of the communication tube (57) to recover regeneration heat. A regeneration heat recovery device 59 is further attached.

The regenerative heat recovery apparatus 59 does not exemplify a specific regenerative heat recovery apparatus because the thermoelectric sensor for converting heat into electricity or various known means capable of utilizing the regenerative heat may be used universally.

In addition, in the cremation system (2) of the contaminated gas removal structure according to an embodiment of the present invention, the temperature, pressure, and the amount of exhaust gas are controlled to a predetermined value in association with the devices of each means, and According to the cosmetic treatment control means 70 for controlling the processing speed of the contaminant removing means is provided, the cosmetic treatment control means 70 is the trolley access control means, the blowing control means 24, the temperature control A communication module 72 in communication with each device of the means 32 and the pollutant removal means 43; A data storage unit 76 which stores control data for each device and sequential control data according to sensed values; A key input unit 74 for generating a manual input value for the control signal; The monitor 78 which displays the driving state of each apparatus is comprised.

In particular, the system of the present invention is configured for each part to monitor the state of the front room hall, the machine room, the bone chamber, and the stack of the crematory, and transmits the imaging data to the makeup process control means 70 ( 62) is installed.

Therefore, the furnace system 2 having the contaminant gas removal structure according to the embodiment of the present invention has a fuel injection amount and combustion air injection amount as a whole according to the temperature and pressure of the main combustion furnace 8 and the reburn furnace 12. By controlling, induction of complete combustion in the furnace and control to keep the combustion gas at an appropriate temperature.

In addition, the cremation system (2) of the contaminated gas removal structure is reinforced in accordance with an embodiment of the present invention by sensing the temperature of the combustion gas flowing in the front end of the first and second gas heat exchangers (37, 38), By controlling the injection amount of the cooling gas introduced into the primary and secondary gas heat exchangers 37 and 38 according to the detected temperature, the temperature of the combustion gas flowing into the pollutant removing means 43 is maintained at a preset temperature. By doing so, the active temperature for pollutant removal is maintained. Thus, contaminants are removed at the optimum temperature.

In particular, the cremation system (2) of the contaminated gas removal structure according to an embodiment of the present invention, the first and second gas heat exchanger (37, 38) in communication with the first and second exhaust gas transferred to the first and second treatment First and second filter dust collectors (44,48); By communicating with the primary and secondary filter dust collectors 44 and 48, the catalytic reactor 55 for tertiary treatment of the exhaust gas is configured to communicate in a multi-stage direct connection method, thereby effectively removing contaminants for each component. Conventionally, the dust collector is about to remove contaminants, but almost no contaminant removal effect, on the contrary, the system of the present invention can completely remove the contaminants, which is environmentally friendly and can eliminate the negative view of the crematory. have.

In addition, the crematory system 2 with the contaminant gas removal structure according to an embodiment of the present invention is an automatic control system for each device, and each device is organically linked and controlled to induce optimal complete combustion. At the same time, it is also intended to ensure complete removal of contaminants.

On the other hand, the cremation system with the contaminant gas removal structure according to the embodiment of the present invention is not limited to the above-described embodiment, but various modifications can be made without departing from the technical gist of the present invention.

1 is a side view illustrating a crematory system in which a crematory system having a contaminated gas removal structure is constructed according to an embodiment of the present invention;

Figure 2 is a block diagram showing a cremation system reinforced with a contaminant gas removal structure according to an embodiment of the present invention.

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

4: elders, 6: all rooms,

8: to main combustion, 12 to reburn,

26: blower, 37,38: 1, secondary gas heat exchanger,

39: 3rd gas heat exchanger, 44: 1 primary filter dust collector,

48: secondary filter dust collector, 50: compressed air supply unit.

54: fly ash processing unit, 55: catalyst reactor,

60: A stack.

Claims (12)

A trolley access control means having a crematorium divided into a main combustion furnace and a recombustion furnace and having a heat insulating door that automatically opens and closes with an in-vehicle trolley transfer part therein, is in communication with the recombustion furnace of the crematorium, and the combustion gas of the final stack furnace In the cremation system to exhaust the gas, It is connected to the flue and the communication pipe to the reburn furnace, flows the cooling gas inside to lower the temperature of the exhaust gas to a predetermined temperature, and 1, 2 to lower the combustion gas blown from the reburn furnace to 400 ℃ or more. A secondary gas heat exchanger; It consists of a tertiary gas heat exchanger that drops the combustion gas dropped to 400 ° C. to 250 ° C. to 300 ° C., and the first and second gas heat exchangers have no air dilution, thereby suppressing dioxin resynthesis. A temperature heat exchanger comprising a gas heat exchanger configured to suppress white smoke through a temperature drop, and a temperature sensing unit configured to sense a temperature of the exhaust gas; It is installed between the communication pipe and the gas heat exchanger to the reburn furnace, and installed at the front of the contaminant removal means and the gas heat exchanger and the chimney, respectively, and a blower for attracting the exhaust gas, and a pressure sensing unit for detecting the pressure of the reburn furnace and each communication tube. And a blowing control means including a pressure control unit for controlling the blower at a predetermined pressure; A primary bag filter which firstly processes the exhaust gas transferred and communicated with the heat exchanger, a bag filter which is in communication with the first bag filter and secondaryly processes the exhaust gas, and a bag filter which is in communication with the secondary bag filter Third stage, the ammonia tank to store ammonia, and a circulation pump for supplying ammonia from the ammonia tank is further installed, the catalytic reactor to reduce the nitrogen oxide and white lead through a hydrolysis method of ammonia is connected in multiple stages Pollutant removal means for removing pollutants, including nitrogen oxides, dioxins and white lead from combustion; Polluting gas, characterized in that it comprises a cosmetic treatment control means for controlling the temperature, pressure, exhaust gas amount to a predetermined value in association with the devices of each means, and controlling the processing speed of the pollutant removal means according to the exhaust gas amount A crematory system with reinforced removal structure. The method of claim 1, wherein the gas heat exchanger is configured in connection with a heat exchanger damper control unit for adjusting the injection amount of the cooling gas according to the temperature and the heat exchanger blower is controlled by the heat exchanger damper control unit for controlling the air flow of the cooling air. A crematory system reinforced with a contaminant gas removal structure. delete According to claim 1, wherein the third gas heat exchanger and the heat exchange at the rear end of the communication pipe for communicating the cooling gas heated to the stack; The cremation system of claim 1, further comprising a regeneration heat recovery device for recovering regeneration heat. According to claim 1, wherein the temperature control means is installed at least two or more in the crematory system through the branched communication pipe installed in order to utilize the heat of the appropriate temperature as a renewable energy, characterized in that the makeup is reinforced with contaminant gas removal structure Furnace system. According to claim 1, wherein the secondary filter dust collector is provided with a branch pipe on the upper portion, the secondary slaked lime / activated carbon supply unit for supplying the hydrated lime and activated carbon to the branch pipe is combined, activated carbon and slaked lime is introduced into the branch pipe The cremation system of which the contaminated gas removal structure is reinforced. The method according to any one of claims 1 to 6, wherein the primary bag filter / primary slag lime for recycling the slaked lime and activated carbon filled into the inside of the second bag filter in the front end to the primary bag filter / The cremation system of claim 1, further comprising an activated carbon supply unit. The method of claim 1, wherein the primary and secondary filter dust collecting unit for compressing the air, the air storage tank for storing the compressed air, and the air storage tank connected to the air storage tank to remove the moisture contained in the stored A cremation system with a contaminant gas removal structure characterized in that the air dryer is connected to receive compressed air. According to claim 1, At the lower end of the first and second filter bag is further equipped with a fly ash processing unit for processing fly ash, the polluted gas removal structure characterized in that the discharged fly ash to the outside to compress the treatment. Reinforced crematory system. delete The apparatus of claim 1, wherein the cosmetic treatment control means comprises: a communication module in communication with each device of the vehicle access control means, the air blowing control means, the temperature control means, and the pollutant removal means; A data storage unit for storing control data for each device and sequential control data according to sensed values; A key input unit for generating a manual input value for the control signal; The cremation system of claim 1, further comprising a monitor for displaying the driving state of each device. The apparatus of claim 1, further comprising a CCTV camera configured to monitor the state of the front room hall, the machine room, the bone chamber, and the stack of the crematory, and to transmit image data to the makeup process control means. A crematory system reinforced with a contaminant gas removal structure.

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