KR102317493B1 - Oil extraction device for pyrolysis of combustible waste movable - Google Patents

Abstract

The present invention relates to a portable waste synthetic resin pyrolysis emulsification recycling device capable of recycling waste synthetic resins such as waste plastics and waste styrofoam generated from industrial wastes or building wastes, etc. as recycled oil. It relates to a portable waste synthetic resin pyrolysis and emulsification recycling device that extracts regenerated oil from waste synthetic resin, purifies harmful gas generated when regenerated oil is extracted, and discharges it to the atmosphere.

Description

Portable waste synthetic resin pyrolysis and emulsification recycling device {Oil extraction device for pyrolysis of combustible waste movable}

The present invention relates to a portable waste synthetic resin pyrolysis emulsification recycling device capable of recycling waste synthetic resins such as waste plastics and waste styrofoam generated from industrial wastes or building wastes, etc. as regenerated oil, and heats and melts the waste, and pyrolyzes and melts the molten waste. It relates to a portable waste synthetic resin pyrolysis and emulsification recycling device that extracts regenerated oil from waste synthetic resin, purifies harmful gas generated when regenerated oil is extracted, and discharges it to the atmosphere.

Along with the rapid industrial development, synthetic resin products are being used in various ways in modern society. However, as the perception that these synthetic resin products are the main culprits in environmental pollution at the present time is increasing, interest in recycling waste synthetic resins is increasing, and various methods for recycling waste are being developed.

The waste emulsification device is one of these attempts, and refers to a device that pyrolyzes waste such as waste plastics or waste wires, extracts liquid fuel from the pyrolyzed waste, and treats waste.

Generally, when waste synthetic resin is generated, it is incinerated or landfilled. When incinerated, there is a problem that air pollutants such as dust, hydrogen chloride (HCl), sulfur oxides (SOx), nitrogen oxides (NOx), and dioxins are discharged. In the case of synthetic resin, it was difficult to decompose due to the nature of the synthetic resin, so there were problems such as soil contamination, leachate, and groundwater contamination.

Accordingly, as a method of recycling waste synthetic resins without incineration or landfill, an emulsification method capable of obtaining useful oil by thermally decomposing a thermoplastic synthetic resin that can be thermally decomposed is known, and research and development of the device is being actively conducted.

The conventional waste pyrolysis emulsification apparatus includes a heating furnace for accommodating the waste and a heating device for heating the heating furnace. In the heating furnace, when the waste synthetic resin is put into the furnace and then the inside of the furnace is heated to 300°C to 600°C through a separate heating device, the waste synthetic resin is dissolved and vaporized. During thermal decomposition, gaseous fuel is discharged to the outside. Liquid fuel can be obtained by liquefying the discharged gaseous fuel through a cooling device.

However, the conventional waste pyrolysis and emulsification equipment is not equipped with a device for processing the gas generated when the waste is heated through a heating furnace, so it is treated as a major cause of odor generation and environmental pollution, so it is very difficult to install an emulsification facility. .

In addition, as the heating efficiency of the heating furnace is very low, the production cost of regenerated oil compared to the fuel used in the heating device increases, and the pressure inside the heating furnace heated to a high temperature is lowered, so that the waste synthetic resin can be put into the heating furnace. When there was a problem with the risk of fire and explosion.

Therefore, it is possible to improve the thermal decomposition efficiency of the heating furnace and secure safety, as well as minimize environmental pollution by treating odors and harmful gases, and develop a synthetic resin pyrolysis emulsification device that can further improve the recovery rate of oil recovered from waste synthetic resin This is a necessary situation.

1. Korea Patent No. 10-0949104 'Waste emulsification device' (application date: 2009.06.18) 2. Korea Patent No. 10-0675909, 'Pyrolysis and emulsification apparatus and method of synthetic resin waste' (application date 2006.09.26)

The present invention has been devised to solve the above problems, by pyrolyzing synthetic resin wastes such as waste plastics and waste styrofoam generated from industrial wastes or construction wastes to recover regenerated oil, and to treat harmful gases generated during pyrolysis An object of the present invention is to provide a portable waste synthetic resin pyrolysis and emulsification recycling device that can minimize environmental pollution.

The portable waste synthetic resin pyrolysis and emulsification recycling device of the present invention has an accommodating space (S) therein, and an inlet 110 is formed on one side so that the waste synthetic resin is accommodated in the accommodating space (S) and melts the accommodated waste synthetic resin. a first heating furnace 100; a second heating furnace 200 for receiving the molten solution from the first heating furnace 100 and maintaining a vacuum state inside to extract gaseous extraction gas through anaerobic pyrolysis; a first burner 310 and a second burner 320 for heating the first heating furnace 100 and the second heating furnace 200, respectively; a separation tower 400 receiving the extraction gas extracted from the second heating furnace 200 and separating the extraction gas and impurities contained in the extraction gas; a condensing unit 500 that receives the extracted gas from the separation tower 400 and cools it to generate liquid regenerated oil from the extracted gas; an oil storage unit 600 for receiving the regenerated oil generated from the condensing unit 500 and storing a predetermined amount; A gas processing unit 700 that is connected to the first heating furnace 100 and receives the harmful gas to neutralize the harmful gas generated in the first heating furnace 100 when the waste synthetic resin is melted and discharged to the outside; It is characterized in that it further comprises.

In the present invention, a fuel supply unit 810 for supplying fuel to the first burner 310 and the second burner 320, respectively; When the regenerated oil is delivered to the oil storage unit 600, the first burner 310 and the second burner ( a gas receiving unit 820 for supplying each of the 320; It is provided between the oil storage unit 600 and the gas receiving unit 820 to fill the gas receiving unit 820 with non-condensed gas at a constant pressure, and when the filling of the gas receiving unit 820 is completed, the and a gas charging unit 830 for discharging the condensed gas to the gas processing unit 700 or the atmosphere.

In addition, the gas processing unit 700 of the present invention has a hollow inside and a receiving case 710 that receives harmful gas from the first heating furnace 100; a neutralizing agent storage unit 720 for supplying a neutralizing solution to the inside of the receiving case 710; a gas delivery pipe 730 through which noxious gas is delivered from the first heating furnace 100, and one end of which is located below the water surface of the neutralizing solution accommodated in the accommodation case 710; a gas discharge pipe 740 provided on one side of the receiving case 710 and discharging the neutralized harmful gas to the atmosphere by reacting with the neutralizing liquid; a cooling module 750 surrounding the outside of the receiving case 710 and cooling the receiving case 710; and an outlet 760 for discharging the neutralizing solution to the outside as the pH concentration of the neutralizing solution accommodated in the receiving case 710 increases.

The inside of the first heating furnace 100 of the present invention is put together with the waste synthetic resin, and when the waste synthetic resin is melted, the impurities contained in the waste synthetic resin move to the second heating furnace 200 It is characterized in that the blocking carrier 900 is further provided.

In addition, the carrier 900 of the present invention has a predetermined thickness and the bottom plate 910 on which the waste synthetic resin is seated; an upper wire 920 spaced apart from the upper side of the bottom plate 910 and enclosing a circumferential surface of the waste synthetic resin; a plurality of connecting wires 930 connecting the bottom plate 910 and the upper wire 920; Including, but the edge of the bottom plate 910 is further provided with fastening grooves 911 formed in the same number as the connecting wires 930 and fixing pins 912 formed in the fastening grooves 911, At one end of the connecting wire 930, a fastening ring 931 that is fastened to the fixing pin 912 and rotates is further provided.

The present invention is provided with a gas processing unit capable of separately processing harmful gases generated as various waste materials are heated together with the waste synthetic resin, and by heating the first heating furnace and the second heating furnace to different temperatures, melting There is an advantage in that only waste synthetic resins having different points can be selected and melted.

In addition, the present invention can first classify impurities contained in the waste synthetic resin through a carrier that is put together with the waste synthetic resin inside the first heating furnace, thereby minimizing impurities in the extracted oil, and at the same time improving oil productivity There are advantages to doing it.

1 is a schematic diagram showing the overall configuration and flow of the present invention.
Figure 2 is a perspective view showing the overall appearance of the present invention.
3 is a cross-sectional view showing the main configuration of the first heating furnace of the present invention.
4 is a cross-sectional view showing the main configuration of a second heating furnace of the present invention.
5 is a schematic diagram showing an embodiment of the present invention;
6 is a cross-sectional view showing the main configuration of the gas processing unit of the present invention.
7 is a perspective view showing a carrier and a first heating furnace of the present invention.

Hereinafter, an embodiment of the portable waste synthetic resin pyrolysis and emulsification recycling apparatus of the present invention will be described in detail with reference to the drawings.

1 and 2, the portable combustible waste pyrolysis and emulsification apparatus of the present invention is a first heating furnace 100, a second heating furnace 200 and each of the first and second heating furnaces 100 and 200 for heating It has a first burner 310 and a second burner 320 .

The first heating furnace 100 has a hollow shape inside and an accommodation space S in which the waste synthetic resin can be accommodated is formed. At this time, an inlet 110 for injecting the waste synthetic resin is formed on one side of the first heating furnace 100 , preferably at the upper end, and the inlet 110 is opened and closed by a separate cover or the like.

The first burner 310 heats the first heating furnace 100 to a temperature of 330° C. or less. This is to remove the melting and moisture and harmful gas of the waste synthetic resin accommodated in the first heating furnace 100 before the waste synthetic resin is transferred to the second heating furnace 200 where full-scale thermal decomposition is performed. And, the temperature of the first heating furnace 100 can be easily changed according to the user's selection.

Since non-combustible materials such as glass and metal are mixed in the waste synthetic resin mixed with various types of waste, these non-combustible materials are screened during the melting and transfer process made in the first heating furnace 100, and only synthetic resins are selectively It has the advantage of being able to melt.

The second heating furnace 200 is connected to the first heating furnace 100 , and receives the molten solution molten in the first heating furnace 100 . The second heating furnace 200 is heated through the second burner 320 in order to heat the melt that has moved to the second heating furnace 200 for thermal decomposition, and the melt accommodated in the second heating furnace 200 is heated. As it is heated, the gaseous extraction gas is extracted from the molten liquid.

At this time, in the second heating furnace 200, anaerobic thermal decomposition proceeds and the inside is maintained in a vacuum state. That is, when the anaerobic pyrolysis proceeds when the melt is pyrolyzed, the extraction efficiency of the gas is improved, and the leakage of the extracted gas can be prevented.

On the other hand, an opening/closing means for opening and closing the inside of the second heating furnace 200 may be separately provided on one side of the second heating furnace 200 , which discharges residues and the like inside the second heating furnace 200 . It can be used as a means to

Another embodiment of the first heating furnace 100 and the second heating furnace 200 will be described with reference to FIGS. 3 and 4 .

The first heating furnace 100 is a first casing 120 in which the waste synthetic resin is accommodated, and a first hot air housing 130 that surrounds the outside of the first casing 120 while being spaced apart from the outer surface of the first casing 120 by a predetermined distance. ) is further included. The first burner 310 is installed on one side of the first hot air housing 130 , and the hot air (thermal energy) transmitted from the first burner 310 is transferred to the outer surface of the first casing 120 and the first hot air housing 130 . ) to heat the first casing 120 while moving along the spaced apart space.

In this case, the first hot air housing 130 may further include a spiral first hot air guide plate 131 for guiding the transmitted hot air and a hot air outlet 132 through which the hot air is discharged. Through this, as the contact time between the first casing 120 and the hot air is increased, there is an advantage in that the loss of heat energy for heating the first casing 120 can be minimized.

The second heating furnace 200 also surrounds the second casing 220 while being spaced apart from the second casing 220 and the outer surface of the second casing 220 to receive the molten solution, and a second burner 320 is provided on one side. It includes a second hot air housing 230 to be connected. And, the second hot air housing 230 may be provided with a second hot air guide plate 231 forming a spiral, and a hot air outlet 232 for discharging the hot air moving along the second hot air guide plate 231 to the outside. do. This is the same as the effect of the first hot air guide plate 131, so a detailed description will be omitted.

In addition, a separate cooling unit for cooling the second heating furnace 200 may be additionally provided at one side of the second heating furnace 200 . This is to prevent the risk of fire and explosion when the residual carbide is discharged after the completion of pyrolysis of the second heating furnace 200 . The cooling unit may be a water cooling type, an air cooling type, etc., but in the present invention, an air cooling technique for cooling the second heating furnace 200 by spraying air at room temperature from the bottom surface of the second heating furnace 200 may be grafted.

And, referring to FIGS. 1 and 2 , a nitrogen supply unit 1000 for supplying nitrogen to the inside of the first heating furnace 100 and the second heating furnace 200 may be further provided. That is, the inside of the first heating furnace 100 and the second heating furnace 200 is in a vacuum state as the waste synthetic resin is melted and the harmful gas of the first heating furnace 100 and the extraction gas of the second heating furnace 200 are discharged. and as the vacuum state is maintained, the emission efficiency of harmful gas and extraction gas gradually decreases.

To compensate for this, by supplying nitrogen to the first heating furnace 100 and the second heating furnace 200, respectively, it is possible to keep the discharge efficiency of harmful gas and extracted gas constant, and the first and second heating furnaces ( 100,200) can keep the internal atmospheric pressure equal to the external atmospheric pressure. In addition, when the first and second heating furnaces 100 and 200 are opened, there is an additional advantage that can prevent the risk of explosion while the outside air flows into the first and second heating furnaces 100 and 200 .

The nitrogen supplied to the first heating furnace 100 is discharged to the outside through the gas processing unit 700 , or discharged to the outside when the first heating furnace 100 is opened, and the nitrogen supplied to the second heating furnace 200 . is discharged to the outside when the second heating furnace 200 is opened, or is accommodated in an oil storage unit 600 to be described below and discharged to the outside, or is classified as non-condensed gas and is first through a gas receiving unit 820 to be described below. And it may be transferred to the second burner (310, 320) to be discharged to the outside.

1 and 4, a separation tower 400 that receives the extraction gas extracted from the second heating furnace 200 and separates the extraction gas and impurities contained in the extraction gas, respectively, is further provided, and the separation tower ( A condensing unit 500 that receives the extract gas from 400 and cools the extract gas to generate liquid regenerated oil from the extract gas is further provided. The condensing unit 500 includes a first condensing unit 510 and a second condensing unit 520 . The first condensing unit 510 receives the extraction gas from which impurities are removed from the separation tower 400 and cools the extraction gas so that the extraction gas is generated as liquid oil.

The second condensing unit 520 is a second condensing unit 520 for secondarily cooling the liquid regenerated oil to prevent ignition and danger as the liquid regenerated oil extracted from the first condensing unit 510 maintains a high temperature. A condensing unit 520 is further provided. That is, when the regenerated oil produced by the liquid regenerated oil passes through the second condensing unit 520 and is cooled in the first condensing unit 510 is stored, the temperature is lowered to reduce the risk of ignition, and the liquefaction of the extracted gas is stored. efficiency can be increased.

A storage tank 600 for receiving and storing the cooled regenerated oil generated by the second condensing unit 520 is further provided. The storage tank 600 is located at the lower end of the condensing unit 500 and stores the regenerated oil that has passed through the second condensing unit 520 . At this time, a flow rate sensor (not shown) may be further provided in the storage tank 600 so that the regenerated oil can be discharged to the outside when a certain amount of regenerated oil is received.

And, referring to FIG. 2 , a controller 1100 for controlling the heating temperature of the first burner 310 and the second burner 320 may be further provided. The control unit 1100 controls the first burner 310 and the second burner 320 to maintain the same internal temperature of the first heating furnace 100 and the second heating furnace 200 or to have different temperatures. control the operation.

And, referring to FIGS. 1 and 2 , a cooling water supply unit 530 for supplying cooling water to the first condensing unit 510 and the second condensing unit 520 may be further provided. The first condensing unit 510 and the second condensing unit 520 are respectively connected to the cooling water supply unit 530 to receive cooling water. At this time, in order to improve the cooling efficiency of the first condensing unit 510 and the second condensing unit 520 , cooling water is circulated between the first condensing unit 510 and the second condensing unit 520 and the cooling water supply unit 530 . A distributor 532 connected to the supply pump 531 and the supply pump 531 to distribute the cooling water to the first condensing unit 510 and the second condensing unit 520 may be further provided.

At this time, the temperature of the cooling water passing through the first condensing unit 510 and the second condensing unit 520 is increased, and heat exchange is performed by a separate chiller 540 connected to the cooling water supply unit 530 to cool the cooling water again. As this is done, the temperature of the high-temperature coolant is lowered.

On the other hand, referring to FIGS. 1, 5, and 6 , a gas processing unit that is connected to the first heating furnace 100 to neutralize the harmful gas generated in the first heating furnace 100 and discharge the harmful gas to the outside ( 700) is further provided. The gas processing unit 700 can prevent harmful gas generated when the waste synthetic resin is melted in the first heating furnace 100 from being directly discharged to the outside, and can prevent air pollution by purifying and treating the harmful gas.

The gas processing unit 700 includes an accommodating case 710 , a neutralizing agent storage unit 720 , a gas delivery pipe 730 , a gas discharge pipe 740 and a cooling module 750 , and an outlet 760 provided at the lower end of the accommodating case 710 . ) is included.

The receiving case 710 receives the neutralizing liquid from the neutralizing agent storage unit 720 and has a hollow shape inside to accommodate the neutralizing liquid, and receives the harmful gas from the first heating furnace 100, and the harmful gas is Since it corresponds to hydrogen chloride (HCL) and water (H2O), the neutralization solution may correspond to a basic aqueous solution (sodium hydroxide: NaOH) or water. The neutralizing agent storage unit 720 is connected to the receiving case 710 to supply the neutralizing solution so that a predetermined amount of the neutralizing solution can be accommodated in the receiving case 710 .

The gas delivery pipe 730 has a hollow tube shape inside to receive harmful gas from the first heating furnace 100 , and one end is located under the water surface of the neutralizing solution accommodated in the receiving case 710 , and the other end It is connected to this first heating furnace 100 . Accordingly, the noxious gas is accommodated inside the housing case 710 while in contact with the neutralizing solution, and the noxious gas reacts with the neutralizing solution to complete the neutralization.

The gas discharge pipe 740 is provided on one side of the receiving case 710, and as the gas discharge pipe 740 is opened and closed, the neutralized harmful gas can be discharged into the atmosphere, and preferably a pressure valve that is opened when a certain pressure is applied. can be

The cooling module 750 surrounds the outside of the receiving case 710 , and receives cooling water from the distributor 532 to cool the outside of the receiving case 710 . That is, since the harmful gas is heated to a high temperature, the temperature of the housing case 710 is increased, and thus the neutralization efficiency may be lowered. Therefore, the temperature of the housing case 710 may be lowered through the cooling module 750 .

And, as the pH concentration of the neutralizing solution accommodated in the receiving case 710 increases, the neutralizing solution and the precipitate generated due to the neutralization reaction are discharged through the outlet 760, and the neutralizing agent storage unit 720 by the discharged amount You can replenish the neutralizer.

In order to accommodate a certain amount of neutralizing solution inside the receiving case 710, the receiving case 710 is further provided with a flow gauge and a Ph concentration meter capable of detecting the amount of neutralizing solution, and a flow gauge and a neutralizing agent storage unit ( 720) may be connected to the control unit 1100 to continuously replenish the lost neutralization solution to maintain neutralization efficiency.

Referring to FIG. 1 , the non-condensed gas that has not been condensed in the fuel supply unit 810 and the condenser unit 500 for supplying fuel to the first burner 310 and the second burner 320, respectively, is used as an auxiliary fuel, etc. For this purpose, a gas receiving unit 820 for supplying each of the first burner 310 and the second burner 320 is further provided. That is, when the regenerated oil is delivered to the oil storage unit 600, the non-condensed gas that is not condensed in the condensing unit 500 is stored in the oil storage unit 600, and the non-condensed gas is used in the first and second burners ( 310,320) as fuel.

At this time, a gas filling unit 830 provided between the oil storage unit 600 and the gas receiving unit 820 to supply the non-condensed gas to the gas receiving unit 820 is further provided. The gas charging unit 830 fills the gas accommodating unit 820 with non-condensed gas at a constant pressure, and when the filling of the gas accommodating unit 820 is completed, the non-condensed gas is discharged to the gas processing unit 700 or the atmosphere. For this reason, the gas accommodating unit 820 is always uniformly filled with non-condensed gas, and even when the fuel supply unit 810 runs out of fuel, the first and second burners 310 and 320 can be used for a predetermined time.

Referring to Figure 7, the inside of the first heating furnace 100 is further provided with a carrier 900 that is put together with the waste synthetic resin. When the waste synthetic resin is melted, impurities contained in the waste synthetic resin are primarily filtered to block the impurities from moving to the second heating furnace 200, and the waste synthetic resin seated on the carrier 900 through a separate crane or the like. is put into the first heating furnace 100 .

The carrier 900 includes a bottom plate 910 , an upper wire 920 and a connecting wire 930 . The bottom plate 910 has a plate shape having a predetermined thickness and is seated on the upper surface of the waste synthetic resin. At this time, a through hole through which the melt of the waste synthetic resin can be moved may be separately formed in the center of the bottom plate 910 , and the entire bottom plate 910 may be formed in a mesh shape including a plurality of through holes. Accordingly, impurities of a certain size that have not been melted may be filtered out of the bottom plate 910 , and the filtered impurities are removed after withdrawing from the first heating furnace 100 in order to input the next synthetic resin.

The upper wire 920 is spaced apart from the upper side of the bottom plate 910 by a predetermined interval, and is formed to surround the circumferential surface of the waste synthetic resin. The wire of the crane may be fastened to the upper wire 920 . And the connecting wire 930 connects the bottom plate 910 and the upper wire 920, and a plurality of them are formed along the edge of the bottom plate 910 .

At this time, the binding groove 911 formed in the same number as the connection wire 930 is formed at the edge of the bottom plate 910 , and a cylindrical fixing pin 912 is further provided in the binding groove 911 . Accordingly, a fastening ring 931 fastened to the fixing pin 912 may be further provided at one end of the connection wire 930 , and the fastening ring 931 is coupled and fixed to surround the outside of the fixing pin 912 . It can be rotated at a predetermined angle while maintaining a state coupled to the pin 912 . Therefore, even if the bottom plate 910 is twisted at high temperature or deformed in shape, it is possible to prevent the phenomenon that the connection portion of the connection wire 930 is easily damaged.

According to the present invention by such a configuration, it is possible to maintain a pleasant ambient air environment by separately treating harmful gases, to minimize impurities in extracted oil, and to improve oil productivity.

100: first heating furnace 200: second heating furnace
310: first burner 320: second burner
400: separation tower 510: first condensing unit
520: second condensing unit 600: oil storage unit
700: gas processing unit 810: fuel supply unit
820: gas receiving unit 830: gas charging unit
900: carrier

Claims (5)

a first heating furnace 100 having an accommodation space S formed therein, an inlet 110 formed on one side so that the waste synthetic resin is accommodated in the accommodation space S, and melting the accommodated waste synthetic resin;
a second heating furnace 200 for receiving the molten solution from the first heating furnace 100 and maintaining a vacuum state inside to extract gaseous extraction gas through anaerobic pyrolysis;
a first burner 310 and a second burner 320 for heating the first heating furnace 100 and the second heating furnace 200, respectively;
a separation tower 400 receiving the extraction gas extracted from the second heating furnace 200 and separating the extraction gas and impurities contained in the extraction gas;
a condensing unit 500 receiving the extracted gas from the separation tower 400 and cooling it to generate liquid regenerated oil from the extracted gas;
an oil storage unit 600 for receiving the regenerated oil generated from the condensing unit 500 and storing a predetermined amount;
a gas processing unit 700 connected to the first heating furnace 100 to neutralize the harmful gas generated in the first heating furnace 100 when the waste synthetic resin is melted and discharged to the outside to receive the harmful gas;
A carrier that is put together with the waste synthetic resin inside the first heating furnace 100 and blocks impurities contained in the waste synthetic resin from moving to the second heating furnace 200 when the waste synthetic resin is melted. (900); is further provided,
The carrier 900 has a predetermined thickness and the bottom plate 910 on which the waste synthetic resin is seated;
an upper wire 920 spaced apart from the upper side of the bottom plate 910 and enclosing a circumferential surface of the waste synthetic resin;
a plurality of connecting wires 930 connecting the bottom plate 910 and the upper wire 920; including,
The edge of the bottom plate 910 is further provided with a fixing groove 911 formed in the same number as the connection wire 930 and a fixing pin 912 formed in a cylindrical shape in the engagement groove 911,
A mobile waste synthetic resin pyrolysis and emulsification recycling device, characterized in that at one end of the connecting wire (930), a fastening ring (931) that is fastened to surround the outside of the fixing pin (912) and rotates is further provided. The method of claim 1,
a fuel supply unit 810 for supplying fuel to the first burner 310 and the second burner 320, respectively;
When the regenerated oil is delivered to the oil storage unit 600, the first burner 310 and the second burner ( a gas receiving unit 820 for supplying each of the 320;
It is provided between the oil storage unit 600 and the gas receiving unit 820 to fill the gas receiving unit 820 with non-condensed gas at a constant pressure, and when the gas receiving unit 820 is completely charged, the a gas charging unit 830 for discharging the condensed gas to the gas processing unit 700 or the atmosphere;
A portable waste synthetic resin pyrolysis emulsification recycling device comprising a. The method of claim 1,
The gas processing unit 700 has a hollow inside, the receiving case 710 to receive the harmful gas from the first heating furnace 100;
a neutralizing agent storage unit 720 for supplying a neutralizing solution to the inside of the receiving case 710;
a gas delivery pipe 730 through which noxious gas is delivered from the first heating furnace 100, one end of which is located below the water surface of the neutralizing solution accommodated in the accommodation case 710;
a gas discharge pipe 740 provided on one side of the receiving case 710 and for discharging the neutralized harmful gas to the atmosphere by reacting with the neutralizing liquid;
a cooling module 750 surrounding the outside of the accommodating case 710 and cooling the accommodating case 710;
an outlet 760 for discharging the neutralizing solution to the outside as the pH concentration of the neutralizing solution accommodated in the receiving case 710 increases;
A portable waste synthetic resin pyrolysis emulsification recycling device comprising a. delete delete

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