Plastic degradation device

Abstract

The invention provides a plastic degradation device which comprises a solar photoelectric conversion system, a storage battery, a light condensation device, a reactor, a gas generator and a reaction control system, the device uses renewable solar energy as a unique energy source, and other energy and substance input is not needed except water, a catalyst and reaction raw materials; therefore, the conversion of the waste plastic completely driven by solar energy can be realized. The solar photoelectric conversion system can realize zero carbon emission in the whole reaction process, and can convert the waste plastics into high-quality fuel and chemical raw materials. Therefore, according to the plastic degradation device provided by the invention, the emission of net CO2 in the waste plastic conversion process is reduced, and renewable energy-driven and environment-friendly waste plastic recycling is realized.

Description

Technical Field

[0001] The present application relates to the technical field of degradable plastics, and in particular to a device for degrading plastics. Background Art

[0002] At present, the methods for degrading waste plastics, in addition to physical methods such as incineration and landfill, are mainly focused on chemical methods such as pyrolysis and hydrogenolysis. From the perspective of energy utilization and environmental protection, the currently developed pyrolysis and hydrogenolysis methods have many problems, mainly: limited by the characteristics of waste plastics themselves that are difficult to transform, the pyrolysis and hydrogenolysis processes consume a lot of energy, and the value of the converted products is less than the cost of raw materials, separation process and energy input; most of the energy comes from thermal power plants, and after overall accounting, it is still a process with a net carbon emission greater than zero. However, the annual amount of waste plastics generated worldwide has reached 100 million tons. The use of traditional hydrogenolysis and pyrolysis methods for recycling is not only inefficient, but may even lead to more CO2 emissions. Therefore, how to reduce energy loss and save costs while realizing the recycling and transformation of waste plastics, and realize a green and environmentally friendly process is an important issue that must be solved in the large-scale recycling of waste plastics. Summary of the invention

[0003] The purpose of this application is to provide a device for degrading plastics to reduce net CO2 emissions during the conversion of waste plastics and achieve renewable energy-driven, environmentally friendly recycling of waste plastics.

[0004] The present application provides a device for degrading plastics, which includes a solar photovoltaic conversion system, a storage battery, a light concentrator, a reactor, a gas generator, and a reaction control system;

[0005] The solar photovoltaic conversion system is electrically connected to the gas generator, the reaction control system, and the storage battery respectively;

[0006] The light concentrator focuses sunlight onto the reactor;

[0007] The reactor is connected to the gas generator through an air inlet pipeline, and the reactor is connected to the gas collector through an air outlet pipeline;

[0008] The reaction control system is electrically connected to the reactor and the light focusing device respectively to control and record reaction parameters; the reaction parameters include the temperature of the reactor and the light intensity provided by the light focusing device.

[0009] In some embodiments of the present application, the focusing device includes a focusing mirror and an adjustment module, and the angle of the focusing mirror or the distance between the focusing mirror and the reactor is controlled by adjusting the adjustment module.

[0010] In some embodiments of the present application, the gas generator is selected from a hydrogen or nitrogen gas generator.

[0011] In some embodiments of the present application, the temperature of the reactor is 50-450°C.

[0012] In some embodiments of the present application, the temperature of the reactor is 250-450°C.

[0013] In some embodiments of the present application, the solar photovoltaic conversion system is electrically connected to the gas generator, the reaction control system, and the battery respectively after passing through the transformer.

[0014] In some embodiments of the present application, the solar photovoltaic conversion system includes a solar panel, and the solar panel is equipped with an automatic light tracker.

[0015] In some embodiments of the present application, a pressure control valve is provided on the air intake pipeline.

[0016] In some embodiments of the present application, the reaction control system is electrically connected to the pressure control valve to control and record the gas flow in the intake pipeline.

[0017] In some embodiments of the present application, a back pressure valve is provided on the air outlet pipeline.

[0018] Beneficial effects of this application:

[0019] The present application provides a device for degrading plastics, including a solar photovoltaic conversion system, a storage battery, a focusing device, a reactor, a gas generator, and a reaction control system. The device uses renewable solar energy as the only energy source, and does not require any other energy and material input except water, catalysts, and reaction raw materials, so as to achieve the conversion of waste plastics completely driven by solar energy. The solar photovoltaic conversion system can achieve "zero carbon emissions" in the entire reaction process and convert waste plastics into high-quality fuels and chemical raw materials. Therefore, the device for degrading plastics provided by the present application reduces the net CO2 emissions in the process of converting waste plastics, and realizes the recycling of waste plastics driven by renewable energy and in an environmentally friendly manner.

[0020] Of course, any product implementing the present application does not necessarily need to achieve all of the advantages described above at the same time. BRIEF DESCRIPTION OF THE DRAWINGS

[0021] In order to more clearly illustrate the technical solutions in the embodiments of the present application, the drawings required for use in the description of the embodiments will be briefly introduced below. Obviously, the drawings described below are only some embodiments of the present application, and a person skilled in the art can also obtain other embodiments based on these drawings.

[0022] Figure 1 The figure is a schematic diagram of the structure of a device for degrading plastics;

[0023] Among them, 1 is a solar photovoltaic conversion system, 2 is a battery, 3 is a focusing device, 4 is a reactor, 5 is a gas generator, 6 is a reaction control system, 7 is a gas collector, 8 is a transformer, 9 is an automatic light chaser, 10 is a pressure control valve, and 11 is a back pressure valve. DETAILED DESCRIPTION

[0024] The following will be combined with the drawings in the embodiments of the present application to clearly and completely describe the technical solutions in the embodiments of the present application. Obviously, the described embodiments are only part of the embodiments of the present application, rather than all the embodiments. All other embodiments obtained by those skilled in the art based on the present application belong to the scope of protection of the present application.

[0025] The present application provides a device for degrading plastics, which includes a solar photovoltaic conversion system, a storage battery, a light concentrator, a reactor, a gas generator, and a reaction control system;

[0026] The solar photovoltaic conversion system is electrically connected to the gas generator, the reaction control system, and the storage battery respectively;

[0027] The light concentrator focuses sunlight onto the reactor;

[0028] The reactor is connected to the gas generator through an air inlet pipeline, and the reactor is connected to the gas collector through an air outlet pipeline;

[0029] The reaction control system is electrically connected to the reactor and the light focusing device respectively to control and record reaction parameters; the reaction parameters include the temperature of the reactor and the light intensity provided by the light focusing device.

[0030] In the present application, there is no particular restriction on the type of battery, as long as it can achieve the purpose of the present application. For example, an outdoor battery with a battery capacity of 2000-4000 watt-hours (Wh) and an input power of 1000-5000W can be selected.

[0031] The present application provides a plastic degradation device which uses renewable solar energy as the only energy source, thereby reducing net CO2 emissions during the conversion of waste plastics and achieving renewable energy-driven, environmentally friendly recycling of waste plastics.

[0032] In some embodiments of the present application, the gas generator is selected from a hydrogen or nitrogen gas generator.

[0033] In some embodiments of the present application, the focusing device includes a focusing mirror and an adjustment module, and the angle of the focusing mirror or the distance between the focusing mirror and the reactor is controlled by adjusting the adjustment module.

[0034] In the present application, there is no particular restriction on the type of condenser, as long as it can achieve the purpose of the present application. For example, a lens with a focal length of 200-800 mm can be selected.

[0035] In the present application, by regulating the adjustment module, the angle of the condenser or the distance between the condenser and the reactor is controlled, and thus the temperature of the reactor can be controlled to meet the temperature requirement for plastic degradation.

[0036] In some embodiments of the present application, the regulating module includes a motor and a computer program.

[0037] The inventors discovered during their research that by setting a thermocouple feedback temperature on the reactor, a computer program can make judgments and instruct the motor to move the condenser, thereby changing the distance between the reactor and the condenser, thereby controlling the temperature of the reactor to meet the temperature requirements for plastic degradation.

[0038] In some embodiments of the present application, the temperature of the reactor is 50-450°C.

[0039] In some embodiments of the present application, the temperature of the reactor is 250-450°C.

[0040] The inventors found in the research that by adjusting the adjustment module, controlling the angle of the condenser or the distance between the condenser and the reactor, the temperature of the reactor can be controlled within 50-450°C, and most plastics can be degraded within this temperature range. For example, polyolefin plastics and polyester plastics can be degraded. Preferably, the polyolefin plastic is selected from at least one of polyethylene plastics, polypropylene plastics, polystyrene plastics and polyvinyl chloride plastics; the polyester plastic is selected from at least one of polyethylene terephthalate plastics, polycarbonate plastics, polyurethane plastics and polylactic acid plastics.

[0041] In some embodiments of the present application, the solar photovoltaic conversion system is electrically connected to the gas generator, the reaction control system, and the storage battery after passing through the transformer. In the present application, the solar photovoltaic conversion system converts solar energy into electrical energy, and the electrical energy is supplied to the gas generator and the reaction control system after passing through the transformer, and / or stored in the storage battery.

[0042] In some embodiments of the present application, the solar photovoltaic conversion system includes a solar panel, and the solar panel is equipped with an automatic light tracker.

[0043] Solar panels are devices that absorb sunlight and convert solar radiation energy directly or indirectly into electrical energy through photoelectric effect or photochemical effect. When many solar panels are connected in series or in parallel, they can form a solar cell array with relatively large output power. In this application, there is no particular restriction on the number and type of solar panels, as long as the purpose of this application can be achieved. For example, solar panels with a total output power of 50-300W can be selected.

[0044] In some embodiments of the present application, the automatic light chaser includes a photoresistor, a computer program, and a motor.

[0045] The inventor discovered in the research that the solar panel is equipped with an automatic light chaser, which realizes the light chasing function of the solar panel through a photoresistor, a computer program and a motor. The computer program monitors the resistance of the photoresistor located at the center of the solar panel in real time, and drives the motor to rotate in four directions, up, down, left and right, to find the minimum point of the photoresistor resistance, and repeat the above steps until it is less than the set threshold, so as to maximize the efficiency of solar power generation.

[0046] In some embodiments of the present application, a pressure control valve is provided on the air intake pipeline.

[0047] In some embodiments of the present application, the reaction control system is electrically connected to the pressure control valve to control and record the gas flow in the intake pipeline.

[0048] In some embodiments of the present application, a back pressure valve is provided on the air outlet pipeline.

[0049] In some embodiments of the present application, a device for degrading plastic is provided, such as Figure 1 As shown, it includes a solar photovoltaic conversion system 1, a storage battery 2, a concentrating device 3, a reactor 4, a gas generator 5, and a reaction control system 6;

[0050] The solar photovoltaic conversion system 1 comprises a solar panel, and the solar panel is equipped with an automatic light chaser 9 .

[0051] The solar photovoltaic conversion system 1 converts solar energy into electrical energy, which is supplied to the gas generator 5 and the reaction control system 6 after passing through the transformer 8, and the remaining electrical energy is stored in the storage battery 2;

[0052] The light concentrator 3 focuses the sunlight onto the reactor 4 to obtain the heat energy required for the reaction;

[0053] The reactor 4 has an air inlet pipeline and an air outlet pipeline; the air inlet pipeline is connected to the gas generator 5, and the gas generated by the gas generator 5 enters the reactor 4 through the air inlet pipeline; the air outlet pipeline is connected to the gas collector 7;

[0054] The gas generator 5 is selected from a gas generator of hydrogen or nitrogen;

[0055] A pressure control valve 10 is provided on the pipeline between the gas generator 5 and the gas inlet of the reactor 4; a back pressure valve 11 is provided on the pipeline connecting the gas outlet of the reactor 4 and the gas collector 7;

[0056] The reaction control system 6 is electrically connected to the reactor 4, the focusing device 3, and the pressure control valve 10, respectively, to control and record the reaction parameters; the reaction parameters include the temperature of the reactor 4, the light intensity provided by the focusing device 3, and the gas flow rate of the air inlet pipeline;

[0057] The device for degrading plastics of the present application has an output electrical power that is greater than the sum of the power used by the gas generator 5 and the reaction control system 6 .

[0058] The present application also provides a method for degrading plastic using the device for degrading plastic of the present application, comprising the following steps:

[0059] Mix the plastic and the catalyst and load them into the reactor;

[0060] The mass ratio of the plastic to the catalyst is 1-5:1; the catalyst is selected from metal-loaded Al2O3, TiO2, CeO2, SiO2, etc.; the metal is selected from Pt, Ru, Rh, Ni, Pd or Ir;

[0061] Turn on the solar photovoltaic conversion system to supply the generated electricity to the gas generator, the reaction control system, and the battery. The hydrogen generated by the gas generator enters the reactor from the air inlet pipeline of the reactor for hydrogenolysis reaction, and CH4 and HCl are collected in the gas collector; wherein the mass ratio of CH4 to HCl is 9-17:1; or,

[0062] The nitrogen generated by the gas generator enters the reactor from the gas inlet pipeline of the reactor for pyrolysis reaction, and is collected in the gas collector to obtain C3-C 10 Alkanes and C6-C 10 Aromatic hydrocarbons; wherein the C3-C 10 Alkanes and C6-C 10 The mass ratio of aromatics is 1:1.2-2;

[0063] The temperature of the reactor is controlled by controlling the angle of the condenser or the distance between the condenser and the reactor. The temperature of the reactor is 50-450°C, preferably 250-450°C.

[0064] In some embodiments of the present application, C3-C 10 Alkanes include propane, propylene, butane, pentane and their isomers, C6-C10 Aromatic hydrocarbons include benzene, toluene, ethylbenzene, etc. and their isomers.

[0065] In some embodiments of the present application, the device for degrading plastic is used for degrading polyolefin plastic and polyester plastic. Preferably, the polyolefin plastic is selected from at least one of polyethylene plastic, polypropylene plastic, polystyrene plastic and polyvinyl chloride plastic; the polyester plastic is selected from at least one of polyethylene terephthalate plastic, polycarbonate plastic, polyurethane plastic and polylactic acid plastic.

[0066] In some embodiments of the present application, the chemical reaction formula of the hydrogenolysis reaction is:

[0067] CO x Cl y H z +(2+x+y / 2-z / 2)H2=CH4+xH2O+yHCl.

[0068] The device for degrading plastic provided in the present application and the method for degrading plastic using the device for degrading plastic provided in the present application reduce the net CO2 emission during the conversion of waste plastics and realize the environmentally friendly recycling of waste plastics driven by renewable energy.

[0069] Example

[0070] The following examples are given to more specifically describe the embodiments of the present application. Various tests and evaluations were performed according to the following methods. In addition, unless otherwise specified, "parts" and "%" are based on mass.

[0071] Calculation of conversion rate

[0072] Conversion rate = 100% - the number of moles of the remaining mixed waste plastics / the number of moles of the input mixed waste plastics × 100%;

[0073] Among them, for a single type of plastic, the molar number is the molar number corresponding to the monomer of its polymer. During the experiment, the mixed waste plastics were weighed separately for each plastic and then mixed. The molar number of mixed waste plastics put into the mixed waste plastics was the sum of the molar numbers of several plastics put in, and the molar number of the remaining mixed waste plastics was the sum of the molar numbers of several plastics remaining after degradation was completed.

[0074] Calculation of output

[0075] During the degradation reaction, a gas collector is used to collect gas from the reactor outlet pipe, and the gas is detected by the flame ionization detector (FID) and thermal conductivity detector (TCD) in the gas chromatograph. The product yield is calculated by the chromatographic peak area and the corresponding response factor of the product, as well as the argon (Ar) internal standard response factor. Taking methane as an example: n(CH4) is the amount of methane, n(Ar) is the amount of Ar (injected into the gas chromatograph at the same time as methane); X(CH4) is the relative response factor of methane, and X(Ar) is the relative response factor of Ar:

[0076]

[0077] Calculation of yield

[0078] The yield is the ratio of the actual output of the product obtained from a unit amount of mixed waste plastics to the theoretically calculated maximum output of the product obtained from a unit amount of mixed waste plastics.

[0079] Taking CH4 as an example, CH4 yield = actual CH4 mole number obtained / theoretical maximum CH4 mole number × 100%; wherein, the theoretical maximum CH4 mole number is the mole number of carbon atoms in the mixed waste plastics.

[0080] The structure of the device for degrading plastics used in the following embodiments is as follows:

[0081] The solar photovoltaic conversion system consists of two 1.0m×0.5m square ethylene-tetrafluoroethylene copolymer (ETFE) flexible solar panels (Dongguan Kupa Technology Co., Ltd., model KUPA-100W; peak power 100W); the ETFE flexible solar panels are equipped with automatic light chasers (Shenzhen Taoyouqu Technology Co., Ltd., model A1), which realize the light chasing function of the solar panel through photoresistors, computer programs and motors; the solar photovoltaic conversion system is connected to a transformer (Guangzhou Changji Electronics Co., Ltd., model 2000W), and the transformer is respectively connected to a gas generator (Shanghai Aikun Instrument Equipment Co., Ltd., model AK-H300), a reaction control system (MEACON, model MIK-200D, 6 channels) and a battery (60Ah / 4400W outdoor battery, Dongguan Kupa Technology Co., Ltd.); the reactor is a cylindrical glass tube with an inner diameter of about 1.5cm, with an air inlet pipe and an air outlet pipe on the top, the air inlet pipe is connected to the gas generator, the air outlet pipe is connected to the gas collector, a pressure control valve is arranged on the air inlet pipe, and a back pressure valve is arranged on the air outlet pipe; the reaction control system connects the pressure control valve, the reactor and the focusing device; the focusing device includes a focusing mirror and an adjustment module, the focusing mirror is a Fresnel lens (Meiying Technology, size 1.1m×1.1m, focal length 620mm), and the adjustment module is temperature-controlled by a total solar irradiance sensor (Shandong Jianda Renke Electronic Technology Co., Ltd., RS-RA-*-JT) to keep the reactor temperature in a relatively stable range as much as possible.

[0082] Performance evaluation of a device for degrading plastics

[0083] After field testing, it was found that the above-mentioned plastic degradation device can output a maximum electrical power of about 200W, which is sufficient to drive the gas generator (rated power 100W) and the reaction control system (rated power 50W) with a large margin, and can achieve self-sustaining operation.

[0084] The focusing heat generation performance of the focusing device under actual sunlight was evaluated below, and the results are shown in Table 1 below.

[0085] Table 1 Concentrating heat generation capacity of concentrating devices under different sunlight intensities

[0086]

[0087] As can be seen from Table 1, the sunlight intensity is between 410-620 W·m -2 , the reactor temperature can reach 250-360°C, indicating that the light concentrator of the present application has a strong light concentrating heat generating capability. Moreover, the inventors found during the test that the reactor of the present application can maintain a constant temperature for a certain period of time.

[0088] Example 1

[0089] 0.8g polyethylene, 0.8g polypropylene, 0.2g polyvinyl chloride, and 0.4g catalyst Ni / Al2O3 were mixed and loaded into the reactor. The solar photovoltaic conversion system was turned on to supply the generated electricity to the gas generator and the reaction control system. The hydrogen generated by the gas generator through the electrolysis of water entered the reactor from the reactor's air inlet pipe for hydrogenolysis reaction. The reaction control system controlled the temperature of the reactor by controlling the angle of the condenser or the distance between the condenser and the reactor; the reaction control system controlled the flow rate of hydrogen entering the reactor to 20mL / min; the reaction was continued for 7 days, and 1787mg CH4 and 113mg HCl were collected in the gas collector after 7 days; the CH4 yield was 87%, and the HCl yield was 98%. The specific parameters and results are shown in Table 2.

[0090] Example 2

[0091] 2g polyethylene and 2g polypropylene were mixed with 1.0g catalyst Ni / Al2O3 and loaded into the reactor. The solar photovoltaic conversion system was turned on to generate electricity to supply the gas generator and the reaction control system. The nitrogen generated by the gas generator entered the reactor from the air inlet of the reactor for pyrolysis reaction. The reaction control system controlled the temperature of the reactor by controlling the angle of the condenser or the distance between the condenser and the reactor. The reaction control system controlled the flow rate of hydrogen entering the reactor to be 20mL / min. The reaction was continued for 7 days. After 7 days, 1318mg C3-C 10 Alkanes and 2244 mg C6-C 10 Aromatics; C3-C 10 The alkane yield was 33%, C6-C 10 The aromatics yield was 61.1%. Specific parameters and results are shown in Table 3.

[0092] Since solar energy is the only energy source for the plastic degradation device of the present application, the intensity of sunlight has a great influence on the reaction effect of the plastic degradation device of the present application on degrading plastic. Examples 1 and 2 of the present application tested the degradation and conversion of waste plastics by the plastic degradation device under different sunlight intensities, and the results are shown in Tables 2 and 3.

[0093] Table 2 Results of the hydrogenolysis experiment of the plastic degradation device for mixed waste plastics

[0094]

[0095]

[0096] Note: “-” in Table 2 means no corresponding parameter.

[0097] The inventors found in the study that when the light intensity is high, the reactor can be heated to above 350°C, while when the light intensity is low, the temperature of the reactor can only be heated to about 270-290°C. As can be seen from Table 2, the plastic degradation device of the present application can achieve effective conversion of waste plastics: when the light intensity is high, a higher yield of CH4 and HCl can be obtained, and when the light intensity is low, the yield of CH4 and HCl is slightly lower. After 7 days of operation, 1.8g of waste plastics are completely converted to produce 1787mg of CH4 and 113mg of HCl, achieving a CH4 yield of more than 80% and a HCl yield of more than 95%.

[0098] Table 3 Results of the pyrolysis experiment of mixed waste plastics using the plastic degradation device

[0099]

[0100] Note: “-” in Table 3 means no corresponding parameter.

[0101] The inventors found that the reaction control system can control the angle of the condenser or the distance between the condenser and the reactor to control the temperature of the reactor to 250-350°C, and different proportions of C3-C 10 Alkanes and C6-C 10 Aromatic hydrocarbons. At 250℃-300℃, the alkane yield is relatively high, and the alkane: aromatic hydrocarbon carbon number ratio is about 0.8-1:1; at 300℃-350℃, the aromatic hydrocarbon yield is relatively high, and the alkane: aromatic hydrocarbon carbon number ratio is about 0.6-0.7:1. As can be seen from Table 3, the plastic degradation device of the present application can effectively transform waste plastics: when the light intensity is high, a high yield of C3-C 10 Alkanes and C6-C 10 Aromatic hydrocarbons; when the light intensity is low, the C3-C 10 Alkanes and C6-C 10 The yield of aromatics was slightly lower. After 7 days of operation, 4 g of waste plastic was completely converted to produce 1318 mg of C3-C 10 of alkanes and 2244 mg of C6-C 10 Aromatic hydrocarbons have achieved a waste plastic conversion rate of more than 95%.

[0102] In summary, the plastic degradation device provided by the present application solves the defect that the previous waste plastic recycling process mainly relies on power supply from the power grid. It uses renewable solar energy as the only energy source. Except for water, catalysts and reaction raw materials, no other energy and material input is required, and the conversion of waste plastics completely driven by solar energy can be achieved. The solar photovoltaic conversion system can work stably, achieve "zero carbon emissions" in the entire reaction process, and convert waste plastics into high-quality fuels and chemical raw materials. Therefore, the plastic degradation device provided by the present application reduces the net CO2 emissions in the waste plastic conversion process, and realizes the renewable energy-driven, environmentally friendly recycling of waste plastics.

[0103] The above description is only a preferred embodiment of the present application and is not intended to limit the present application. Any modifications, equivalent substitutions, improvements, etc. made within the spirit and principles of the present application shall be included in the scope of protection of the present application.

Claims

1. A device for degrading plastics, comprising a solar photovoltaic conversion system, a storage battery, a light concentrator, a reactor, a gas generator, and a reaction control system; The solar photovoltaic conversion system is electrically connected to the gas generator, the reaction control system, and the storage battery respectively; The light concentrator focuses sunlight onto the reactor; The reactor is connected to the gas generator through an air inlet pipeline, and the reactor is connected to the gas collector through an air outlet pipeline; The reaction control system is electrically connected to the reactor and the light focusing device respectively to control and record reaction parameters; the reaction parameters include the temperature of the reactor and the light intensity provided by the light focusing device.

2. The device according to claim 1, wherein: The focusing device comprises a focusing mirror and an adjustment module. The angle of the focusing mirror or the distance between the focusing mirror and the reactor is controlled by adjusting the adjustment module.

3. The device according to claim 1, wherein: The gas generator is selected from a hydrogen or nitrogen gas generator.

4. The device according to claim 1, wherein: The temperature of the reactor is 50-450°C.

5. The device according to claim 4, wherein: The temperature of the reactor is 250-450°C.

6. The device according to claim 1, wherein: The solar photovoltaic conversion system is electrically connected to the gas generator, the reaction control system and the storage battery respectively after passing through the transformer.

7. The device according to claim 1, wherein: The solar photovoltaic conversion system comprises a solar panel, and the solar panel is equipped with an automatic light chaser.

8. The device according to claim 1, wherein: A pressure control valve is arranged on the air intake pipeline.

9. The device according to claim 8, wherein: The reaction control system is electrically connected to the pressure control valve to control and record the gas flow of the intake pipeline.

10. The device according to claim 1, wherein: A back pressure valve is arranged on the air outlet pipeline.

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