Flue gas sampler capable of automatically sampling and collecting
By controlling the input rate and negative pressure reaction of the hydrogen peroxide solution through an automatic flue gas sampler and combining it with a PLC system, the problem of uncontrollable concentration in flue gas sampling is solved, and dynamic adjustment and safe and efficient sampling are achieved.
Patent Information
- Application Number
- CN202510880418.4
- Authority / Receiving Office
- CN · China
- Patent Type
- Applications(China)
- Current Assignee / Owner
- Filing Date
- 2025-06-27
- Publication Date
- 2025-10-21
AI Technical Summary
In existing flue gas sampling technology, the concentration is uncontrollable. Traditional methods require an external dilution device to adjust the sampling gas concentration and flow rate, and dynamic adjustment cannot be achieved.
The flue gas sampler with automatic sampling and collection is used to control the input rate of hydrogen peroxide solution, combined with the negative pressure reaction component and PLC control system to achieve dynamic adjustment of flue gas concentration and flow.
It achieves precise control of flue gas concentration and flow, protects the health and safety of operators, and improves sampling efficiency and real-time data.
Smart Images

Figure CN120820375A_ABST
Abstract
Description
Technical Field
[0001] The invention belongs to the technical field of flue gas sampling, and in particular relates to a flue gas sampler for automatic sampling and collection. Background Art
[0002] Flue gas sampling refers to the process of collecting flue gas samples from industrial emissions or ambient air for analysis of their composition, concentration, and pollutant characteristics, providing data support for environmental monitoring, pollution control, and regulatory compliance. Sampling methods are primarily categorized as direct sampling and dilution sampling. Direct sampling involves extracting flue gas through a probe into a sampling container or analytical instrument. It is suitable for high-temperature, high-humidity, or corrosive gases. Commonly used equipment includes a flue gas sampling gun, condenser, and filter. Dilution sampling involves diluting the flue gas with clean air to reduce its temperature and concentration. It is suitable for collecting respirable particulate matter (PM2.5, PM10) or volatile organic compounds (VOCs). Commonly used equipment includes a dilution tunnel and cyclone separator. Factors such as flue gas temperature, pressure, flow rate, and oxygen content must be considered during sampling to ensure sample representativeness and accuracy. Isokinetic sampling is a key technique, which adjusts the sampling flow rate to match the flue gas flow rate to avoid distorted particle distribution. Condensation and adsorption losses must also be prevented during sampling, typically using heated sampling lines or inert materials. Common analytical items include sulfur dioxide (SO2), nitrogen oxides (NOx), carbon monoxide (CO), particulate matter (PM), and heavy metals. Flue gas sampling is widely used in industrial fields such as thermal power plants, steel mills, and chemical plants, as well as in motor vehicle exhaust detection and indoor air quality assessment. Standardized sampling processes and instrument calibration are key to ensuring data reliability and must comply with national or international standards such as the EPA Method and ISO 12141. With technological advances, online monitoring and portable sampling equipment have become increasingly popular, improving sampling efficiency and real-time performance, and providing a scientific basis for environmental pollution control and emission reduction policymaking.
[0003] In the existing technology, the concentration of flue gas sampling is uncontrollable. The traditional sampling method requires an external dilution device to adjust the concentration of the sampled gas, which is inconvenient to control the concentration and flow of the sampled flue gas, and dynamic adjustment cannot be achieved when sampling. Summary of the Invention
[0004] The purpose of the present invention is to provide a flue gas sampler for automatic sampling and collection, aiming to solve the problem that the concentration of flue gas sampling in the existing technology is uncontrollable. The traditional sampling method requires an external dilution device to achieve concentration adjustment of the sampled gas, which is inconvenient to control the concentration and flow of the sampled flue gas, and cannot achieve dynamic adjustment when sampling.
[0005] To achieve the above object, the present invention provides the following technical solutions:
[0006] A flue gas sampler for automatic sampling and collection, comprising:
[0007] Sampler body;
[0008] A water inlet cavity, the water inlet cavity being provided in the sampler body;
[0009] A reaction chamber is provided in the sampler body and is connected to the water inlet chamber through a water inlet channel;
[0010] An inverted conical channel, the inverted conical channel is opened in the sampler body, the inverted conical channel is arranged on the lower side of the reaction chamber, the inverted conical channel is connected to the water inlet chamber through the air transmission channel, and the inverted conical channel is connected to the reaction chamber through the negative pressure channel;
[0011] a storage bottle, the storage bottle being threadedly connected to the sampler body;
[0012] an exhaust channel, the exhaust channel being opened in the sampler body and communicating with the reaction chamber; and
[0013] A negative pressure reaction component includes reactants, a filling catalyst, a metal mesh and a heating plate. The reactants are placed in a storage bottle, the metal mesh is slidably connected to the sampler body, the metal mesh is connected to the reaction chamber, the filling catalyst is installed in the metal mesh, the heating plate is fixedly connected to the sampler body, and the heating plate is connected to the reaction chamber.
[0014] As a preferred solution of the present invention, the reactant is a hydrogen peroxide solution, the filling catalyst is manganese dioxide particles, a fifth control valve is provided in the exhaust channel, and the fifth control valve is a PTFE valve.
[0015] As a preferred solution of the present invention, a sampling bottle is provided on the lower side of the sampler body, a knob is rotatably connected to the surface of the sampling bottle, the knob is threadedly connected to the sampler body, and a strap is provided on the surface of the sampling bottle.
[0016] As a preferred solution of the present invention, an air intake pipe is fixedly connected to the sampler body, and the air intake pipe is connected to the water inlet chamber. An external frame is fixedly connected to the surface of the sampler body, and an external pipe is fixedly connected to the external frame, and the external pipe is fixedly connected to one end of the air intake pipe.
[0017] As a preferred solution of the present invention, a filter plate is provided in the sampler body, and the filter plate is connected to the air intake pipe.
[0018] As a preferred solution of the present invention, a first control valve, a fourth control valve, a second control valve and a third control valve are installed in the sampler body, a drainage channel is opened in the sampler body, the drainage channel is connected to the water inlet chamber, the first control valve is connected to the drainage channel, the fourth control valve is connected to the gas transmission channel, the second control valve is connected to the water inlet channel, and the third control valve is connected to the negative pressure channel.
[0019] As a preferred solution of the present invention, a nozzle is installed in the sampler body, and the nozzle is connected to the reaction chamber and the storage bottle. A pump body is installed in the sampler body, and the pump body is connected to the gas transmission channel.
[0020] As a preferred solution of the present invention, a first slider is slidably connected inside the sampler body, and the first slider is connected to the filter plate. A second slider is slidably connected inside the sampler body, and the second slider is connected to the power module. A crash barrier is fixedly connected to the surface of the sampler body.
[0021] As a preferred solution of the present invention, the lower end of the sampler body is fixedly connected to a crawler body.
[0022] As a preferred solution of the present invention, a power module is installed in the sampler body, and the power module is electrically connected to the first control valve, the fourth control valve, the second control valve, the third control valve, the fifth control valve, the nozzle, the track body and the pump body.
[0023] Compared with the prior art, the present invention has the following beneficial effects:
[0024] 1. In the present invention, by using this device, the input of hydrogen peroxide solution is controlled, the reaction rate of hydrogen peroxide is directly controlled, and the effect of controlling the negative pressure and the flow rate of flue gas absorbed by the negative pressure is achieved, which is convenient for controlling the concentration and flow rate of the sampled flue gas and realizing dynamic adjustment.
[0025] 2. In the present invention, the power module, the first control valve, the fourth control valve, the second control valve, the third control valve, the fifth control valve, the nozzle, the track body and the pump body are all controlled by a PLC control system. Through the control of this system, the movement of the automatic control device and the collection of smoke are controlled; the PLC control system is used to prevent people from inhaling smoke and protect their health and safety.
[0026] 3. In the present invention, the nozzle sprays out the hydrogen peroxide solution output from the storage bottle. Through this design, the contact area between the hydrogen peroxide solution and the manganese dioxide is increased, and the reaction rate of the hydrogen peroxide solution is improved. The pump body is used to provide partial pressure when the pressure in the inverted tapered channel is insufficient, so that smoke will not remain in the device. BRIEF DESCRIPTION OF THE DRAWINGS
[0027] The accompanying drawings are used to provide a further understanding of the present invention and constitute a part of the specification. Together with the embodiments of the present invention, they are used to explain the present invention and do not constitute a limitation of the present invention. In the accompanying drawings:
[0028] Figure 1 This is a first perspective stereogram of the present invention;
[0029] Figure 2 This is a second perspective stereogram of the present invention;
[0030] Figure 3 It is the front view of the present invention;
[0031] Figure 4 is a side view of the present invention;
[0032] Figure 5 is a cross-sectional view of the present invention;
[0033] Figure 6 For the present invention Figure 5 A partial enlarged view of point A in the middle;
[0034] Figure 7 For the present invention Figure 5 A partial enlarged view of point B in the middle;
[0035] Figure 8 For the present invention Figure 5 A partial enlarged view of point C in the middle.
[0036] In the figure: 1. Track body; 2. Sampler body; 3. Water inlet chamber; 301. Sensor; 302. Drainage channel; 303. First control valve; 4. Air inlet pipe; 401. Filter plate; 402. First slider; 403. External frame; 404. External pipe; 5. Power module; 501. Second slider; 6. Water inlet channel; 601. Second control valve; 7. Reaction chamber; 701. Heating plate; 702. Metal mesh; 703. Sealing block; 704. Negative pressure channel; 705. Third control valve; 8. Gas transmission channel; 801. Fourth control valve; 802. Pump body; 803. Inverted cone channel; 804. Knob; 9. Sampling bottle; 901. Strap; 10. Exhaust channel; 1001. Fifth control valve; 1002. Dustproof plate; 11. Storage bottle; 1101. Nozzle; 12. Anti-collision guardrail. DETAILED DESCRIPTION
[0037] The following will clearly and completely describe the technical solutions in the embodiments of the present invention in conjunction with the accompanying drawings. Obviously, the described embodiments are only part of the embodiments of the present invention, not all of the embodiments. Based on the embodiments of the present invention, all other embodiments obtained by ordinary technicians in this field without making creative efforts are within the scope of protection of the present invention.
[0038] Example 1
[0039] See also Figures 1-8 , the present invention provides the following technical solutions:
[0040] A flue gas sampler for automatic sampling and collection, comprising:
[0041] Sampler body 2;
[0042] A water inlet chamber 3 is provided in the sampler body 2;
[0043] The reaction chamber 7 is provided in the sampler body 2 and is connected to the water inlet chamber 3 through the water inlet channel 6;
[0044] The inverted conical channel 803 is opened in the sampler body 2 and is arranged on the lower side of the reaction chamber 7. The inverted conical channel 803 is connected to the water inlet chamber 3 through the gas transmission channel 8 and is connected to the reaction chamber 7 through the negative pressure channel 704.
[0045] A storage bottle 11 is threadedly connected to the sampler body 2;
[0046] An exhaust channel 10 is provided in the sampler body 2 and is connected to the reaction chamber 7; and
[0047] The negative pressure reaction component includes reactants, a filling catalyst, a metal mesh 702 and a heating plate 701. The reactants are placed in the storage bottle 11, the metal mesh 702 is slidably connected to the sampler body 2, the metal mesh 702 is connected to the reaction chamber 7, the filling catalyst is installed in the metal mesh 702, the heating plate 701 is fixedly connected to the sampler body 2, and the heating plate 701 is connected to the reaction chamber 7.
[0048] In a specific embodiment of the present invention, the water inlet chamber 3 opened in the sampler body 2 is used to store the water source generated after the reaction of the negative pressure reaction component. The water source is input into the water inlet chamber 3 through the water inlet channel 6. The height of the water is higher than the air inlet pipe 4. The flue gas input from the air inlet pipe 4 is washed with water and then input into the sampling bottle 9 through the air transmission channel 8 and the inverted cone channel 803 to complete the collection of the flue gas. The reaction chamber 7 is used for the reaction of the reactants and the filling catalyst in the negative pressure reaction component. The storage bottle 11 is used to store the reactants. The reaction in the negative pressure reaction component The reactant is input into the reaction chamber 7 through the nozzle 1101, and the nozzle 1101 sprays the reactant on the surface of the metal mesh 702. Under the action of the heating plate 701 and the filled catalyst, the hydrogen peroxide decomposes to produce oxygen and water. The water is input into the water inlet chamber 3 through the water inlet channel 6 and is used for water washing of the flue gas. The oxygen is discharged to the outside through the exhaust channel 10 and the fifth control valve 1001. After the oxygen is discharged, the negative pressure in the reaction chamber 7 acts on the inverted cone channel 803 and the sampling bottle 9 through the negative pressure channel 704. The inverted cone channel 803 and The pressure in the sampling bottle 9 decreases, and the flue gas washed with water in the water inlet chamber 3 enters the sampling bottle 9 through the gas transmission channel 8 and the inverted cone channel 803 and is collected by the sampling bottle 9; an auxiliary pump is provided in the nozzle 1101, and the auxiliary pump pumps the hydrogen peroxide solution stored in the storage bottle 11 out through the nozzle 1101 and sprays it on the surface of the metal mesh 702. When the auxiliary pump is not running, the hydrogen peroxide solution in the storage bottle 11 cannot be sprayed out from the nozzle 1101; a sensor 301 is also fixedly connected to the sampler body 2, and the sensor 301 is connected to the water inlet chamber 3 connection, is used to detect the pH value of the water source in the water inlet chamber 3. The acid and alkaline components in the flue gas enter the water, making the water acidic or alkaline. When the acidity or alkalinity exceeds the threshold value detected by the sensor 301, the first control valve 303 is controlled to open, and the water in the water inlet chamber 3 is discharged through the drainage channel 302. By using this device, the input of the hydrogen peroxide solution is controlled, and the reaction rate of the hydrogen peroxide is directly controlled, so as to achieve the effect of controlling the negative pressure and the flow rate of the flue gas absorbed by the negative pressure, which is convenient for controlling the concentration and flow rate of the sampled flue gas and realizing dynamic regulation.
[0049] For details, please refer to Figures 1-8 The reactant is hydrogen peroxide solution, the filling catalyst is manganese dioxide particles, and a fifth control valve 1001 is provided in the exhaust channel 10. The fifth control valve 1001 is a PTFE valve.
[0050] In this embodiment: hydrogen peroxide solution is for industrial use and is inexpensive. The sealing block 703 has a cavity structure, and manganese dioxide particles are filled in the cavity. A plurality of holes are provided on the surface of the sealing block 703, and the manganese dioxide particles cannot pass through the holes. The hydrogen peroxide solution can contact the manganese dioxide particles in the cavity. The fifth control valve 1001 is a PTFE valve, which is a one-way valve and is only used for the passage of oxygen generated by the decomposition of hydrogen peroxide. A dustproof plate 1002 is installed in the sampler body 2 to prevent dust from entering the exhaust channel 10.
[0051] For details, please refer to Figures 1-8 A sampling bottle 9 is provided on the lower side of the sampler body 2. A knob 804 is rotatably connected to the surface of the sampling bottle 9. The knob 804 is threadedly connected to the sampler body 2. A strap 901 is provided on the surface of the sampling bottle 9.
[0052] In this embodiment: the sampling bottle 9 is used to collect smoke. The sampling bottle 9 is threadedly connected to the sampler body 2 through the knob 804. This connection facilitates the installation and removal of the sampling bottle 9. When removing the sampling bottle 9 from the lower surface of the sampler body 2, first use the strap 901 to tie it on the surface of the sampling bottle 9 so that the sampling bottle 9 is not connected to the inverted conical channel 803, and then turn the knob 804 to remove the sampling bottle 9 from the lower surface of the sampler body 2.
[0053] For details, please refer to Figures 1-8 An air intake pipe 4 is fixedly connected to the sampler body 2, and the air intake pipe 4 is communicated with the water inlet chamber 3. An external frame 403 is fixedly connected to the surface of the sampler body 2, and an external tube 404 is fixedly connected to the external frame 403, and the external tube 404 is fixedly connected to one end of the air intake pipe 4.
[0054] In this embodiment, external smoke is input into the water in the water inlet chamber 3 through the external pipe 404 and the air inlet pipe 4 , and the external frame 403 is used to fix the external pipe 404 .
[0055] For details, please refer to Figures 1-8 A filter plate 401 is provided in the sampler body 2 , and the filter plate 401 is connected to the air intake pipe 4 .
[0056] In this embodiment, the filter plate 401 is used to filter the smoke input into the air intake pipe 4 and filter out large particles in the smoke.
[0057] For details, please refer to Figures 1-8The first control valve 303, the fourth control valve 801, the second control valve 601 and the third control valve 705 are installed in the sampler body 2. A drainage channel 302 is opened in the sampler body 2. The drainage channel 302 is connected to the water inlet chamber 3. The first control valve 303 is connected to the drainage channel 302, the fourth control valve 801 is connected to the gas transmission channel 8, the second control valve 601 is connected to the water inlet channel 6, and the third control valve 705 is connected to the negative pressure channel 704.
[0058] In this embodiment: the first control valve 303 is used to control the connectivity state of the drainage channel 302, the fourth control valve 801 is used to control the connectivity state in the gas transmission channel 8, the second control valve 601 is used to control the connectivity state in the water inlet channel 6, and the third control valve 705 is used to control the connectivity state in the negative pressure channel 704.
[0059] For details, please refer to Figures 1-8 A nozzle 1101 is installed in the sampler body 2, and the nozzle 1101 is connected to the reaction chamber 7 and the storage bottle 11. A pump body 802 is installed in the sampler body 2, and the pump body 802 is connected to the gas transmission channel 8.
[0060] In this embodiment, the nozzle 1101 sprays the hydrogen peroxide solution output from the storage bottle 11. This design increases the contact area between the hydrogen peroxide solution and the manganese dioxide, thereby improving the reaction rate of the hydrogen peroxide solution. The pump body 802 is used to provide partial pressure when the pressure in the inverted tapered channel 803 is insufficient, so that smoke will not remain in the device.
[0061] For details, please refer to Figures 1-8 A first slider 402 is slidably connected inside the sampler body 2, and the first slider 402 is connected to the filter plate 401. A second slider 501 is slidably connected inside the sampler body 2, and the second slider 501 is connected to the power module 5. A crash barrier 12 is fixedly connected to the surface of the sampler body 2.
[0062] In this embodiment: the first slider 402 is slidably connected to the sampler body 2, and the first slider 402 is connected to the filter plate 401. Through the sliding connection, it is convenient to remove the filter plate 401 from the sampler body 2 through the first slider 402 and replace the filter plate 401. The second slider 501 is connected to the power module 5. The second slider 501 is slidably connected to the sampler body 2, and the sliding connection facilitates the installation and disassembly of the power module 5.
[0063] For details, please refer to Figures 1-8 The lower end of the sampler body 2 is fixedly connected to the crawler body 1.
[0064] In this embodiment: the crawler body 1 drives the sampler body 2 to move to the target position for collecting flue gas during operation. The crawler body 1 controls its operation through a PLC control system. The crawler body 1 is an existing technology. The specific model of the crawler body 1 can be selected according to actual needs, and no further details will be given here.
[0065] For details, please refer to Figures 1-8 A power module 5 is installed in the sampler body 2, and the power module 5 is electrically connected to the first control valve 303, the fourth control valve 801, the second control valve 601, the third control valve 705, the fifth control valve 1001, the nozzle 1101, the track body 1 and the pump body 802.
[0066] In this embodiment: the power module 5 is used to provide power for the first control valve 303, the fourth control valve 801, the second control valve 601, the third control valve 705, the fifth control valve 1001, the nozzle 1101, the track body 1 and the pump body 802; the power module 5, the first control valve 303, the fourth control valve 801, the second control valve 601, the third control valve 705, the fifth control valve 1001, the nozzle 1101, the track body 1 and the pump body 802 are all controlled by the PLC control system, and the movement of the automatic control device and the collection of flue gas are controlled by the system; the PLC control system is used to prevent people from inhaling flue gas and protect their health and safety. The PLC control system used in this device is also existing technology and will not be elaborated on here.
[0067] The working principle and use process of the present invention are as follows: first, the crawler body 1 is controlled to operate, and the device is moved to the position where the flue gas sampling is required. During the movement, the auxiliary pump is controlled to operate, and the hydrogen peroxide solution in the storage bottle 11 is pumped into the reaction chamber 7 through the nozzle 1101. Under the operation of the heating plate 701, the heat required for the decomposition of the hydrogen peroxide solution is provided, and the water generated by the decomposition of hydrogen peroxide is input into the water inlet chamber 3 through the water inlet channel 6. After the fifth control valve 1001 is opened, the oxygen in the reaction chamber 7 is discharged to the outside through the exhaust channel 10. After the oxygen is discharged, the pressure in the reaction chamber 7 is reduced, and the negative pressure also acts on the negative pressure channel 704 and the inverted cone channel 8. 03 and the sampling bottle 9, the flue gas is input into the water in the water inlet chamber 3 through the external pipe 404 and the air inlet pipe 4, filtered through the filter plate 401 and the water in the water inlet chamber 3, and input into the sampling bottle 9 from the air transmission channel 8 and the inverted cone channel 803. When the sampling is completed, all valves are closed, the strap 901 is tied to the surface of the sampling bottle 9, and then the knob 804 is rotated to remove the sampling bottle 9 from the lower surface of the sampler body 2; by using this device, the input of hydrogen peroxide solution is controlled, and the reaction rate of hydrogen peroxide is directly controlled, so as to achieve the effect of controlling the negative pressure and absorbing the flue gas flow through the negative pressure, which is convenient for controlling the concentration and flow of the sampled flue gas and realizing dynamic adjustment.
[0068] Finally, it should be noted that the above descriptions are merely preferred embodiments of the present invention and are not intended to limit the present invention. Although the present invention has been described in detail with reference to the aforementioned embodiments, those skilled in the art will be able to modify the technical solutions described in the aforementioned embodiments or substitute equivalents for some of the technical features. Any modifications, equivalent substitutions, and improvements made within the spirit and principles of the present invention shall be included within the scope of protection of the present invention.
Claims
1. A flue gas sampler for automatic sampling and collection, characterized in that: include: Sampler body (2); A water inlet chamber (3), wherein the water inlet chamber (3) is provided in the sampler body (2); A reaction chamber (7), the reaction chamber (7) is provided in the sampler body (2), and the reaction chamber (7) is connected to the water inlet chamber (3) through the water inlet channel (6); An inverted conical channel (803), the inverted conical channel (803) is opened in the sampler body (2), the inverted conical channel (803) is arranged on the lower side of the reaction chamber (7), the inverted conical channel (803) is connected to the water inlet chamber (3) through the air transmission channel (8), and the inverted conical channel (803) is connected to the reaction chamber (7) through the negative pressure channel (704); A storage bottle (11), wherein the storage bottle (11) is threadedly connected to the sampler body (2); An exhaust channel (10), the exhaust channel (10) is opened in the sampler body (2), and the exhaust channel (10) is communicated with the reaction chamber (7); and A negative pressure reaction component includes a reactant, a filling catalyst, a metal mesh (702) and a heating plate (701); the reactant is arranged in a storage bottle (11); the metal mesh (702) is slidably connected to the sampler body (2); the metal mesh (702) is connected to the reaction chamber (7); the filling catalyst is installed in the metal mesh (702); the heating plate (701) is fixedly connected to the sampler body (2); and the heating plate (701) is connected to the reaction chamber (7).
2. The automatic sampling and collection flue gas sampler according to claim 1, characterized in that: The reactant is a hydrogen peroxide solution, the filling catalyst is manganese dioxide particles, and a fifth control valve (1001) is provided in the exhaust channel (10), and the fifth control valve (1001) is a PTFE valve.
3. The automatic sampling and collection flue gas sampler according to claim 2, characterized in that: A sampling bottle (9) is provided on the lower side of the sampler body (2), and a knob (804) is rotatably connected to the surface of the sampling bottle (9), and the knob (804) is threadedly connected to the sampler body (2). A strap (901) is provided on the surface of the sampling bottle (9).
4. The automatic sampling and collection flue gas sampler according to claim 3, characterized in that: An air intake pipe (4) is fixedly connected to the sampler body (2), and the air intake pipe (4) is communicated with the water inlet chamber (3). An external frame (403) is fixedly connected to the surface of the sampler body (2), and an external pipe (404) is fixedly connected to the external frame (403). The external pipe (404) is fixedly connected to one end of the air intake pipe (4).
5. The automatic sampling and collection flue gas sampler according to claim 4, characterized in that: A filter plate (401) is provided in the sampler body (2), and the filter plate (401) is connected to the air intake pipe (4).
6. The automatic sampling and collection flue gas sampler according to claim 5, characterized in that: The sampler body (2) is provided with a first control valve (303), a fourth control valve (801), a second control valve (601) and a third control valve (705). A drainage channel (302) is provided in the sampler body (2). The drainage channel (302) is communicated with the water inlet chamber (3). The first control valve (303) is connected to the drainage channel (302). The fourth control valve (801) is connected to the gas transmission channel (8). The second control valve (601) is connected to the water inlet channel (6). The third control valve (705) is connected to the negative pressure channel (704).
7. The automatic sampling and collection flue gas sampler according to claim 6, characterized in that: A nozzle (1101) is installed in the sampler body (2), and the nozzle (1101) is connected to the reaction chamber (7) and the storage bottle (11). A pump body (802) is installed in the sampler body (2), and the pump body (802) is connected to the gas transmission channel (8).
8. The automatic sampling and collection flue gas sampler according to claim 7, characterized in that: A first slider (402) is slidably connected to the sampler body (2), and the first slider (402) is connected to the filter plate (401). A second slider (501) is slidably connected to the sampler body (2), and the second slider (501) is connected to the power module (5). A crash barrier (12) is fixedly connected to the surface of the sampler body (2).
9. The automatic sampling and collection flue gas sampler according to claim 8, characterized in that: The lower end of the sampler body (2) is fixedly connected to a crawler body (1).
10. The automatic sampling and collection flue gas sampler according to claim 9, characterized in that: A power module (5) is installed in the sampler body (2), and the power module (5) is electrically connected to the first control valve (303), the fourth control valve (801), the second control valve (601), the third control valve (705), the fifth control valve (1001), the nozzle (1101), the track body (1) and the pump body (802).