KR20200063611A - Oil extraction device for pyrolysis of combustible waste movable - Google Patents

Abstract

The present invention relates to a mobile apparatus for pyrolysis, emulsification, and recycle of a waste synthetic resin, capable of recycling the waste synthetic resin such as waste plastics and waste Styrofoam generated from industrial waste or construction waste into recycled oil. Specifically, the present invention relates to a mobile apparatus for pyrolysis, emulsification, and recycle of a waste synthetic resin, which heats and melts waste, thermally decomposes the same for the extraction of recycled oil from a molten waste synthetic resin, purifies harmful gases generated during the extraction of recycled oil and releases the same to the atmosphere.

Description

Removable waste synthetic resin pyrolysis waste recycling device {Oil extraction device for pyrolysis of combustible waste movable}

The present invention relates to a mobile waste synthetic resin pyrolysis and emulsification recycling apparatus capable of recycling waste synthetic resins such as waste plastics and waste styrofoam generated from industrial wastes or construction wastes into recycled oil. The present invention relates to a mobile waste synthetic resin pyrolysis and emulsifying recycling device that extracts regenerated oil from waste synthetic resin and purifies harmful gases generated when extracting regenerated oil and releases it to the atmosphere.

With the rapid development of the industry, products using synthetic resins are used in various ways in modern society. However, with the increasing awareness that the products of these synthetic resins are the main culprit for environmental pollution at the present time, interest in the recycling of waste synthetic resins is increasing, and various methods for recycling waste have been developed.

The waste emulsifying device is one of such attempts, and refers to a device that thermally decomposes waste such as waste plastic or waste wire and extracts liquid fuel from the thermally decomposed waste to treat the waste.

In general, when a waste synthetic resin occurs, it is incinerated or landfilled. When incinerated, air pollutants such as dust, hydrogen chloride (HCl), sulfur oxides (SOx), nitrogen oxides (NOx), and dioxin are discharged. In the case of the synthetic resin, it was difficult to decompose, resulting in problems such as soil contamination, leachate generation, and groundwater contamination.

Accordingly, as a method of recycling the waste synthetic resin without incineration or landfilling, a thermoplastic synthetic resin capable of thermal decomposition is known as an emulsification method capable of thermally decomposing it to obtain useful oils, and research and development of the device is actively being conducted.

Conventional waste pyrolysis and emulsifying apparatus includes a heating furnace for receiving waste and a heating device for heating the heating furnace. When the waste synthetic resin is put inside the heating furnace and the inside of the heating furnace is heated to 300°C to 600°C through a separate heating device, the waste synthetic resin is dissolved and gasified. During pyrolysis, gaseous fuel is discharged to the outside. Liquid fuel can be obtained by liquefying the gaseous fuel discharged through the cooling device.

However, the conventional waste pyrolysis and emulsifying device is very difficult to install an emulsifying facility because it is not equipped with a device for treating gas generated when heating the waste through a heating furnace and is a major cause of odor and environmental pollution. .

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

Accordingly, development of a synthetic resin pyrolysis and emulsifying device capable of improving the thermal decomposition efficiency of the heating furnace and ensuring safety, as well as minimizing environmental pollution by treating odor and harmful gas, and further improving the recovery rate of oil recovered from the waste synthetic resin. This is a necessary situation.

1. Korean Registered Patent No. 10-0949104'Waste Emulsifying Device' (application date 2009.06.18) 2. Korean Registered Patent No. 10-0675909'Synthesis and method for thermal decomposition of synthetic resin waste' (application date 2006.09.26)

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

The movable waste synthetic resin pyrolysis emulsification recycling apparatus of the present invention has an accommodation space (S) formed therein, an inlet (110) is formed on one side so that the waste synthetic resin is accommodated in the accommodation space (S), and the accommodated waste synthetic resin is melted. A first heating furnace 100; A second heating furnace 200 that maintains a vacuum inside so as to extract the gaseous extraction gas by anaerobic pyrolysis by receiving the molten liquid from the first heating furnace 100; A first burner 310 and a second burner 320 respectively heating the first heating furnace 100 and the second heating furnace 200; A separation tower 400 for receiving the extracted gas extracted from the second heating furnace 200 and separating impurities contained in the extracted gas and the extracted gas; A condensation unit 500 that receives the extracted gas from the separation tower 400 and cools it to generate liquid regeneration oil from the extracted gas; An oil storage unit 600 receiving the regenerated oil generated from the condensing unit 500 and storing a predetermined amount; When the waste synthetic resin is melted, it is connected to the first heating furnace 100 so as to neutralize and discharge the harmful gas generated in the first heating furnace 100 to the outside, a gas processing unit 700 receiving the harmful gas; Characterized in that it further comprises.

In the present invention, the fuel supply unit 810 for supplying fuel to the first burner 310 and the second burner 320, respectively; When regenerated oil is delivered to the oil storage unit 600, uncondensed gas that is not condensed in the condensation unit 500 is received from the oil storage unit 600, and the first burner 310 and the second burner ( 320) each of the gas receiving portion 820; It is provided between the oil storage part 600 and the gas receiving part 820 to charge uncondensed gas to the gas receiving part 820 at a constant pressure, and when the gas receiving part 820 is completely charged, It characterized in that it comprises; a gas filling 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 is hollow inside the receiving case 710 receiving harmful gas from the first heating furnace 100; A neutralizing agent storage unit 720 for supplying a neutralizing liquid inside the receiving case 710; A gas delivery pipe 730 through which harmful gas is transmitted from the first heating furnace 100, and one end is located under the surface of the neutralizing liquid accommodated in the receiving case 710; A gas discharge pipe 740 which is provided on one side of the accommodation case 710 and discharges neutralized harmful gas into the atmosphere by reacting with the neutralization liquid; A cooling module 750 surrounding the exterior of the storage case 710 and cooling the storage case 710; It characterized in that it comprises; a discharge port 760 for discharging the neutralizing liquid to the outside as the pH concentration of the neutralizing liquid accommodated in the receiving case 710 is increased.

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

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 a predetermined distance above the bottom plate 910 and surrounding the circumferential surface of the waste synthetic resin; A plurality of connection 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 a fixing groove 911 formed in the same number as the connecting wire 930 and a fixing pin 912 formed in the binding groove 911, One end of the connection wire 930 is characterized in that it is further provided with a fastening ring 931 is rotated by being fastened to the fixing pin 912.

The present invention is provided with a gas processing unit capable of separately treating harmful gases generated by heating various waste materials inputted together with the waste synthetic resin, and melting differently by heating the temperatures of heating the first heating furnace and the second heating furnace differently. There is an advantage in that it is possible to select and melt only waste synthetic resins having different points.

In addition, the present invention can primarily classify impurities contained in the waste synthetic resin through a carrier that is injected with the waste synthetic resin inside the first heating furnace, thereby minimizing the impurities of the extracted oil, and at the same time improving oil productivity. There is an advantage that can be made.

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.
Figure 3 is a cross-sectional view showing the main configuration of the first heating furnace of the present invention.
Figure 4 is a cross-sectional view showing the main configuration of the second heating furnace of the present invention.
Figure 5 is a schematic diagram showing an embodiment of the present invention.
Figure 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 mobile waste synthetic resin pyrolysis emulsification recycling apparatus of the present invention will be described in detail with reference to the drawings.

1 and 2, the mobile combustible waste pyrolysis and emulsifying apparatus of the present invention includes a first heating furnace 100, a second heating furnace 200 and a first heating furnace 100 and 200, respectively. It has one burner 310 and a second burner 320.

The first heating furnace 100 has a hollow shape inside, and a receiving space S in which waste synthetic resin can be accommodated is formed. At this time, on one side of the first heating furnace 100, preferably, an inlet 110 through which a waste synthetic resin can be introduced is formed, 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 lower. This is to remove the molten synthetic resin contained in the first heating furnace 100 and to remove moisture and harmful gases 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 the waste synthetic resin mixed with various kinds of wastes contains non-combustible materials such as glass and metal, the non-combustible materials are screened during melting and transport in the first heating furnace 100, and only synthetic resins are selectively selected. It has the advantage of being able to melt.

The second heating furnace 200 is connected to the first heating furnace 100 and receives molten melt from the first heating furnace 100. The second heating furnace 200 is heated through the second burner 320 so as to heat the molten liquid moved to the second heating furnace 200 to proceed with thermal decomposition, and the molten liquid accommodated in the second heating furnace 200 is As it is heated, gaseous extraction gas is extracted from the melt.

At this time, oxygen-free thermal decomposition proceeds in the second heating furnace 200 and the inside maintains a vacuum state. That is, when pyrolysis of oxygen is performed when pyrolysis of the molten liquid, the extraction efficiency of the gas is improved, and leakage of the extracted gas can be prevented.

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

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 spaced apart a predetermined distance from the outer surface of the first casing 120 and the first casing 120 in which the waste synthetic resin is accommodated, the first hot air housing 130 surrounding the outside of the first casing 120 ). 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 the outer surface of the first casing 120 and the first hot air housing 130 ) While moving along the spaced apart space, the first casing 120 is heated.

At this time, the first hot air housing 130 may be further provided with a spiral first hot air guide plate 131 for guiding the transmitted hot air and a hot air outlet 132 through which hot air is discharged. Through this, as the contact time between the first casing 120 and the hot air increases, an advantage of minimizing the loss of thermal energy heating the first casing 120 occurs.

The second heating furnace 200 also wraps the second casing 220 while being spaced apart from the outer surfaces of the second casing 220 and the second casing 220 receiving the molten liquid, and the second burner 320 is provided on one side. It includes a second hot air housing 230 to be connected. In addition, the second hot air housing 230 may be provided with a second hot air guide plate 231 in a spiral shape, and includes a hot air outlet 232 for discharging hot air moved 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 detailed description thereof will be omitted.

In addition, a separate cooling unit for cooling the second heating furnace 200 may be additionally provided on one side of the second heating furnace 200. This is to prevent the risk of fire and explosion when discharging residual carbides after completion of thermal decomposition of the second heating furnace 200. The cooling unit may be water-cooled, air-cooled, or the like, but in the present invention, air-cooled technology for cooling the second heating furnace 200 by injecting air at room temperature from the bottom surface of the second heating furnace 200 may be grafted.

In addition, 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, inside the first heating furnace 100 and the second heating furnace 200, as the waste synthetic resin melts, the harmful gas of the first heating furnace 100 and the extraction gas of the second heating furnace 200 are discharged, and the vacuum state is generated. And the exhaust efficiency of harmful gas and extracted gas gradually decreases as the vacuum is maintained.

To compensate for this, by supplying nitrogen to the first heating furnace 100 and the second heating furnace 200, respectively, it is possible to maintain a constant discharge efficiency of harmful gas and extracted gas, and the first and second heating furnaces ( 100,200) It is possible to maintain the internal pressure equal to the external pressure. In addition, when the first and second heating furnaces 100 and 200 are opened, an additional advantage of preventing the risk of explosion may occur as external 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 When the second heating furnace 200 is opened, it is discharged to the outside or accommodated in the oil storage unit 600 to be discharged and discharged to the outside, or classified as uncondensed gas, and is the first through the gas receiving portion 820 to be treated. And transferred to the second burners 310 and 320 to be discharged to the outside.

Referring to FIGS. 1 and 4, a separation tower 400 is further provided to receive extracted gas extracted from the second heating furnace 200 and separate impurities contained in the extracted gas and the extracted gas, respectively. 400) is further provided with a condensation unit 500 that receives the extracted gas from the extract gas and cools the extracted gas to generate liquid recovery oil from the extracted gas. The condensation unit 500 includes a first condensation unit 510 and a second condensation unit 520. The first condensation unit 510 receives the extraction gas from which the impurities are removed from the separation tower 400 and cools the extraction gas so that the extraction gas is produced as a liquid oil.

The second condensation unit 520 is a second for cooling the regeneration of the liquid secondary to prevent ignition, danger, etc. as the regeneration oil of the liquid extracted from the first condensation unit 510 maintains a high temperature. The condensation unit 520 is further provided. That is, when storing the regenerated oil generated by cooling the regenerated oil of the liquid in the first condensing unit 510 passing through the second condensing unit 520, the temperature is lowered to reduce the risk of ignition and liquefy the extracted gas. Efficiency can be increased.

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

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

In addition, referring to FIGS. 1 and 2, a cooling water storage 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, to improve the cooling efficiency of the first condensing unit 510 and the second condensing unit 520, the cooling water is circulated between the first condensing unit 510, the second condensing unit 520, and the cooling water supply unit 530. The circulation pump 531 and the circulation pump 531 are connected to the circulation pump 531 to distribute the cooling water to the first condensation unit 510 and the second condensation unit 520, which may be further provided.

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

Meanwhile, referring to FIGS. 1, 5, and 6, a gas processing unit connected to the first heating furnace 100 to receive harmful gas through neutralization of harmful gases generated in the first heating furnace 100 and discharged to the outside ( 700) is further provided. The gas processing unit 700 may prevent the harmful gas generated when the waste synthetic resin is melted in the first heating furnace 100 from being directly discharged to the outside, and purify and process the harmful gas to prevent air pollution.

The gas processing unit 700 includes an accommodation 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 bottom of the storage case 710 ).

The receiving case 710 receives a neutralizing liquid from the neutralizing agent storage unit 720 and forms a hollow inside so as to receive the neutralizing liquid, receives harmful gas from the first heating furnace 100, and the harmful gas 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 a neutralizing solution so that a certain 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 below the surface of the neutralizing liquid accommodated in the receiving case 710, and the other end It is connected to the first heating furnace 100. Therefore, the noxious gas is accommodated inside the accommodating case 710 while being in contact with the neutralization liquid, and the neutralization is completed by the noxious gas reacting with the neutralization liquid.

The gas discharge pipe 740 is provided on one side of the receiving case 710, and the gas discharge pipe 740 can be opened and closed to discharge neutralized harmful gas into the atmosphere, and preferably a pressure valve that opens 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 receiving case 710 increases, and thus, the neutralization efficiency may decrease, so that the temperature of the receiving case 710 can be lowered through the cooling module 750.

Then, as the pH concentration of the neutralizing liquid accommodated in the receiving case 710 increases, the precipitate generated due to the neutralization reaction with the neutralizing liquid is discharged through the outlet 760, and the neutralizing agent storage unit 720 is discharged as much as the discharged amount. You can replenish the neutralizing solution.

In the receiving case 710, a flow gauge and a pH concentration meter capable of detecting the capacity of the neutralizing liquid are additionally provided in the receiving case 710 so that a certain amount of the neutralizing liquid can be accommodated in the receiving case 710. 720) may be connected to the control unit 1100 to maintain the neutralization efficiency by continuously replenishing the lost neutralization liquid.

Referring to FIG. 1, using uncondensed gas that is not condensed in the fuel supply unit 810 and the condensation unit 500 for supplying fuel to the first burner 310 and the second burner 320 as auxiliary fuels, etc. To this end, a gas receiving portion 820 that is respectively supplied to the first burner 310 and the second burner 320 is further provided. That is, when the regenerated oil is transferred to the oil storage unit 600, uncondensed gas that is not condensed in the condensation unit 500 is stored in the oil storage unit 600, and the uncondensed gas is first and second burners ( 310,320).

At this time, a gas charging unit 830 provided between the oil storage unit 600 and the gas receiving unit 820 to supply uncondensed gas to the gas receiving unit 820 is further provided. The gas charging unit 830 charges the gas receiving unit 820 with uncondensed gas at a constant pressure, and when the gas receiving unit 820 is completely charged, discharges the uncondensed gas into the gas processing unit 700 or the atmosphere. Due to this, the gas receiving unit 820 is always filled with a uniform uncondensed gas, and the first and second burners 310 and 320 may be used for a certain time even when the fuel supply unit 810 is exhausted.

Referring to FIG. 7, a carrier 900 that is introduced together with the waste synthetic resin is further provided inside the first heating furnace 100. When the waste synthetic resin is melted, the impurities contained in the waste synthetic resin are first filtered to prevent the impurities from moving into the second heating furnace 200, and the waste synthetic resin seated on the carrier 900 through a separate crane or the like. Is injected 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 is a waste synthetic resin is seated on the upper surface, and forms a plate shape having a predetermined thickness. At this time, in the center of the bottom plate 910, a through hole through which the molten synthetic resin is melted may move, and the entire bottom plate 910 may be formed in a mesh shape including a plurality of through holes. As a result, impurities of a certain size that cannot be melted may be filtered into the bottom plate 910, and then filtered impurities are removed after being withdrawn from the first heating furnace 100 to input the next synthetic resin.

The upper wire 920 is spaced a predetermined distance to the upper side of the bottom plate 910 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. In addition, the connecting wire 930 connects the bottom plate 910 and the top wire 920, and is formed in a plurality along the edge of the bottom plate 910.

At this time, a 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 that is fastened to the fastening pin 912 may be further provided at one end of the connection wire 930, and the fastening ring 931 is coupled to surround the outer side of the fastening pin 912 and fixed. It remains connected to the pin 912 and can be rotated at a predetermined angle. Therefore, even if the bottom plate 910 is distorted or deformed at a high temperature, it is possible to prevent a phenomenon such that the connection portion of the connection wire 930 is easily damaged.

The present invention by such a configuration can treat the harmful gas separately to maintain a pleasant ambient air environment, minimize impurities in the extracted oil, and improve oil productivity.

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

Claims (5)

A receiving space (S) is formed therein, an inlet (110) is formed on one side so that the waste synthetic resin is accommodated in the receiving space (S) and the first heating furnace (100) for melting the received waste synthetic resin;
A second heating furnace 200 that maintains a vacuum inside so as to extract the gaseous extraction gas by anaerobic pyrolysis by receiving the molten liquid from the first heating furnace 100;
A first burner 310 and a second burner 320 respectively heating the first heating furnace 100 and the second heating furnace 200;
A separation tower 400 for receiving the extracted gas extracted from the second heating furnace 200 and separating impurities contained in the extracted gas and the extracted gas;
A condensation unit 500 that receives the extracted gas from the separation tower 400 and cools it to generate liquid regeneration oil from the extracted gas;
An oil storage unit 600 receiving the regenerated oil generated from the condensing unit 500 and storing a predetermined amount;
When the waste synthetic resin is melted, it is connected to the first heating furnace 100 so as to neutralize and discharge the harmful gas generated in the first heating furnace 100 to the outside, a gas processing unit 700 receiving the harmful gas; A movable waste synthetic resin pyrolysis emulsification recycling device further comprising. According to claim 1,
A fuel supply unit 810 for supplying fuel to the first burner 310 and the second burner 320, respectively;
When regenerated oil is delivered to the oil storage unit 600, uncondensed gas that is not condensed in the condensation unit 500 is received from the oil storage unit 600, and the first burner 310 and the second burner ( 320) each of the gas receiving portion 820;
It is provided between the oil storage part 600 and the gas receiving part 820 to charge uncondensed gas to the gas receiving part 820 at a constant pressure, and when the gas receiving part 820 is completely charged, A gas filling unit 830 for discharging condensed gas to the gas processing unit 700 or the air;
Portable waste synthetic resin pyrolysis emulsification recycling apparatus comprising a. According to claim 1,
The gas processing unit 700 has a hollow interior and a receiving case 710 receiving harmful gas from the first heating furnace 100;
A neutralizing agent storage unit 720 for supplying a neutralizing liquid inside the receiving case 710;
A gas delivery pipe 730 through which noxious gas is transmitted from the first heating furnace 100 and one end is located under the surface of the neutralizing liquid accommodated in the receiving case 710;
A gas discharge pipe 740 which is provided on one side of the accommodation case 710 and discharges neutralized harmful gas into the atmosphere by reacting with the neutralization liquid;
A cooling module 750 surrounding the exterior of the storage case 710 and cooling the storage case 710;
An outlet 760 for discharging the neutralizing liquid to the outside as the pH concentration of the neutralizing liquid contained in the receiving case 710 increases;
Portable waste synthetic resin pyrolysis emulsification recycling apparatus comprising a. According to claim 1,
A carrier that is introduced into the first heating furnace 100 together with the waste synthetic resin and prevents impurities contained in the waste synthetic resin from moving to the second heating furnace 200 when the waste synthetic resin is melted. A mobile waste synthetic resin pyrolysis emulsification recycling apparatus, characterized in that it is further provided (900). The method of claim 4,
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 a predetermined distance above the bottom plate 910 and surrounding the circumferential surface of the waste synthetic resin;
A plurality of connection 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 connecting wire 930 and a fixing pin 912 formed in the binding groove 911,
A movable waste synthetic resin pyrolysis and emulsification recycling device, characterized in that one end of the connection wire 930 is further provided with a fastening ring 931 that is fastened and rotates on the fixing pin 912.

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