Efficient flue gas desulfurization environment-friendly device
By designing an efficient flue gas desulfurization and environmental protection device including alkaline solution and clean water, the problem of insufficient absorption in the existing technology is solved by using three adsorption processes, which significantly improves the efficiency and environmental protection of flue gas desulfurization.
Patent Information
- Application Number
- CN202411726612.9
- Authority / Receiving Office
- CN · China
- Patent Type
- Applications(China)
- Current Assignee / Owner
- Filing Date
- 2024-11-28
- Publication Date
- 2025-01-21
AI Technical Summary
The existing flue gas desulfurization technology does not absorb the sulfur-containing gas in the flue gas sufficiently, which can easily cause sulfur-containing gas leakage and lead to environmental damage.
An efficient flue gas desulfurization environmental protection device is designed, including a first adsorption box and a second suction adsorption box, which are filled with alkaline solution and clean water respectively. The alkaline solution is input into the tee through the liquid pumping mechanism to mix with the flue gas to achieve one-time adsorption. Treatment, then secondary adsorption through clean water, and finally third adsorption through activated carbon filters to improve absorption efficiency.
Through the three adsorption processes, the absorption efficiency of sulfur oxides in the flue gas is significantly improved, the quality of the remaining tail gas is improved, the damage to the environment is reduced, and a more efficient flue gas desulfurization effect is achieved.
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Figure CN119327258A_ABST
Abstract
Description
Technical Field
[0001] The invention relates to the technical field of flue gas treatment, and in particular to a high-efficiency flue gas desulfurization and environmentally friendly device. Background Art
[0002] Flue gas desulfurization is widely used in many industries that generate large amounts of sulfur oxide emissions, including but not limited to: Power industry: Coal-fired power plants are the main application area for flue gas desulfurization equipment, because the flue gas generated by coal burning contains a large amount of sulfur dioxide. Iron and steel metallurgical industry: Flue gas generated in the process of iron and steel making, including blast furnaces, converters, coke ovens, etc., also needs to be desulfurized. Chemical industry: Waste gas generated in processes such as coal chemical industry, petrochemical industry, fertilizer, and sulfuric acid production often needs to be desulfurized. Building materials industry: Cement plants, glass plants, etc. also release sulfur-containing flue gas during the production process, which requires flue gas desulfurization equipment for treatment. Non-ferrous metal smelting: Flue gas generated in the smelting process of metals such as lead, zinc, and copper also needs to be desulfurized.
[0003] At present, a single method is often used for flue gas desulfurization. This method does not fully absorb the sulfur-containing gas in the flue gas, which easily causes the leakage of sulfur-containing gas and damages the environment. In order to better solve this problem, we propose an efficient flue gas desulfurization environmentally friendly device. Summary of the invention
[0004] The purpose of the present invention is to solve the shortcomings of the prior art and to propose a high-efficiency flue gas desulfurization environmental protection device.
[0005] In order to achieve the above object, the present invention adopts the following technical solutions:
[0006] A high-efficiency flue gas desulfurization environmental protection device includes a first adsorption box and a second adsorption box. A tee is fixed inside the first adsorption box through a first bracket. A pumping mechanism for inputting liquid into the tee is installed inside the first adsorption box. The tee is connected with an air inlet pipe for inputting gas into the tee. A first exhaust pipe is connected between the first adsorption box and the second adsorption box. The first exhaust pipe is connected with a main pipe, and the main pipe is connected with a plurality of unit pipes. Exhaust holes are opened on the unit pipes. The second adsorption box is connected with a conical hood through the second exhaust pipe. The conical hood is fixed to the second adsorption box through a second bracket, and an activated carbon filter is installed at the port of the conical hood.
[0007] Preferably, the first adsorption box and the second adsorption box are installed on a bottom plate, and rollers are installed at the four bottom corners of the bottom plate.
[0008] Preferably, a brake pad is provided on the roller, and a controller is installed on the base plate.
[0009] Preferably, the liquid extraction mechanism includes a liquid extraction pump, a liquid guide tube, and a spherical mesh cover. The liquid guide tube is connected to a port of a tee. The liquid extraction pump is installed on the pipe section of the liquid guide tube. The liquid extraction pump is installed on the inner wall of the first adsorption box. The port of the liquid guide tube is connected to the spherical mesh cover.
[0010] Preferably, a first high liquid level sensor and a first low liquid level sensor are installed on the inner wall of the first adsorption box, and a second high liquid level sensor and a second low liquid level sensor are installed on the inner wall of the second adsorption box.
[0011] Preferably, the side of the first adsorption box is connected with a first liquid discharge pipe and a first liquid inlet pipe, a first shut-off valve is installed on the pipe section of the first liquid discharge pipe, a second shut-off valve is installed on the pipe section of the first liquid inlet pipe, the side of the second adsorption box is connected with a second liquid discharge pipe and a second liquid inlet pipe, a third shut-off valve is installed on the pipe section of the second liquid discharge pipe, and a fourth shut-off valve is installed on the pipe section of the second liquid inlet pipe.
[0012] Preferably, a microporous atomizing plate is installed in a port of the tee close to the pumping mechanism, and a guide plate is fixed in a port of the tee close to the outlet.
[0013] Preferably, a gas flow meter and a first solenoid valve are installed on the pipe section of the air intake pipe, a second solenoid valve is installed on the pipe section of the first exhaust pipe, and a fourth solenoid valve is installed on the pipe section of the second exhaust pipe.
[0014] Compared with the prior art, the present invention has the following beneficial effects:
[0015] In the present invention, the first adsorption box is filled with alkaline solution, the second adsorption box is filled with clean water, the flue gas enters the tee through the air inlet pipe, the liquid extraction mechanism extracts the alkaline solution and inputs it into the tee, the flue gas and the alkaline solution are mixed in the tee, and the primary adsorption treatment of the flue gas is achieved, the residual tail gas enters the main pipe through the first exhaust pipe, and then is sent to the unit pipe by the main pipe and discharged from the exhaust hole on the unit pipe, the clean water performs secondary adsorption on the flue gas, the residual tail gas enters the cone cover through the second exhaust pipe, and then is output from the cone cover and filtered through the activated carbon filter, and the three adsorptions are achieved. Through a total of three adsorption processes, the absorption efficiency is higher, the quality of the residual tail gas is effectively improved, and the damage to the environment is reduced, which is very environmentally friendly;
[0016] In the present invention, the controller is used to control the electrical part of the entire device for easy management. The first high liquid level sensor and the first low liquid level sensor help to control the alkali liquid level. The second high liquid level sensor and the second low liquid level sensor help to control the clean water level. The microporous atomizing plate can atomize the alkali liquid to facilitate better mixing of the alkali liquid and the flue gas. The guide plate can help mix the alkali liquid and the flue gas. BRIEF DESCRIPTION OF THE DRAWINGS
[0017] Figure 1 This is a schematic structural diagram of a high-efficiency flue gas desulfurization environmental protection device proposed by the present invention;
[0018] Figure 2 A cross-sectional view of a first adsorption box of a high-efficiency flue gas desulfurization environmental protection device proposed by the present invention;
[0019] Figure 3 A cross-sectional view of a second adsorption box of a high-efficiency flue gas desulfurization environmental protection device proposed by the present invention;
[0020] Figure 4 A cross-sectional view of a tee of a high-efficiency flue gas desulfurization environmental protection device proposed by the present invention;
[0021] Figure 5 This is a schematic structural diagram of a conical hood of a high-efficiency flue gas desulfurization environmental protection device proposed by the present invention.
[0022] In the figure: 1 bottom plate, 2 roller, 3 first adsorption box, 4 pumping mechanism, 41 pumping pump, 42 liquid guide tube, 43 spherical mesh cover, 5 three-way, 6 first bracket, 7 air inlet pipe, 8 first exhaust pipe, 9 second adsorption box, 10 main pipe, 11 unit pipe, 12 second exhaust pipe, 13 second bracket, 14 conical cover, 15 controller, 16 first liquid discharge pipe, 17 first shut-off valve, 18 first liquid inlet pipe, 19 second shut-off valve, 20 gas flow meter, 21 first solenoid valve, 22 second solenoid valve, 23 first low liquid level sensor, 24 first high liquid level sensor, 25 guide plate, 26 microporous atomizing plate, 27 second liquid inlet pipe, 28 fourth shut-off valve, 29 second liquid discharge pipe, 30 third shut-off valve, 31 exhaust hole, 32 third solenoid valve, 33 fourth solenoid valve, 34 second low liquid level sensor, 35 second high liquid level sensor, 36 activated carbon filter. DETAILED DESCRIPTION
[0023] The technical solutions in the embodiments of the present invention will be described clearly and completely below in conjunction with the drawings in the embodiments of the present invention. Obviously, the described embodiments are only part of the embodiments of the present invention, rather than all the embodiments.
[0024] Reference Figure 1-5A high-efficiency flue gas desulfurization environmental protection device includes a first adsorption box 3 and a second adsorption box 9. The first adsorption box 3 is filled with an alkaline solution, and the second adsorption box 9 is filled with clean water. A tee 5 is fixed inside the first adsorption box 3 through a first bracket 6. A liquid extraction mechanism 4 for inputting liquid into the tee 5 is installed inside the first adsorption box 3. The tee 5 is connected with an air inlet pipe 7 for inputting gas into the tee 5. A first exhaust pipe 8 is connected between the first adsorption box 3 and the second adsorption box 9. The first exhaust pipe 8 is connected with a main pipe 10. The main pipe 10 is connected with a plurality of unit pipes 11. The unit pipe 11 is provided with an exhaust hole 31. The second adsorption box 9 is connected with a conical cover 14 through a second exhaust pipe 12. The conical cover 14 is fixed to the second adsorption box 9 through a second bracket 13. On the adsorption box 9, an activated carbon filter 27 is installed at the port of the conical cover 14, and the flue gas enters the tee 5 through the air inlet pipe 7. The liquid extraction mechanism 4 extracts the alkaline solution and inputs it into the tee 5. In the tee 5, the flue gas and the alkaline solution are mixed to achieve a primary adsorption treatment of the flue gas. The residual tail gas enters the main pipe 10 through the first exhaust pipe 8, and is then sent into the unit pipe 11 by the main pipe 10 and discharged from the exhaust hole 31 on the unit pipe 11. The clean water performs secondary adsorption on the flue gas, and the residual tail gas enters the conical cover 14 through the second exhaust pipe 12, and is then output from the conical cover 14 and filtered through the activated carbon filter 27 to achieve three adsorptions. Through a total of three adsorption processes, the absorption efficiency is higher, the quality of the remaining tail gas is effectively improved, and the damage to the environment is reduced, which is very environmentally friendly.
[0025] Reference Figure 2 The liquid extraction mechanism 4 includes a liquid extraction pump 41, a liquid guide tube 42, and a spherical mesh cover 43. The liquid guide tube 42 is connected to a port of the tee 5. The liquid extraction pump 41 is installed on the pipe section of the liquid guide tube 42. The liquid extraction pump 41 is installed on the inner wall of the first adsorption box 3. The port of the liquid guide tube 42 is connected to the spherical mesh cover 43. The liquid extraction pump 41 extracts liquid, sucks in alkaline liquid through the spherical mesh cover 43, and then sends it into the tee 5 through the liquid guide tube 42.
[0026] Reference Figure 2 , Figure 3The first adsorption box 3 and the second adsorption box 9 are installed on the bottom plate 1. The bottom four corners of the bottom plate 1 are all equipped with rollers 2, and brake pads are arranged on the rollers 2. The bottom plate 1 is equipped with a controller 15, and the controller 15 is used to control the electrical part of the whole device for convenient management. The first high liquid level sensor 24 and the first low liquid level sensor 23 are installed on the inner wall of the first adsorption box 3. The first high liquid level sensor 24 and the first low liquid level sensor 23 help to control the alkali liquid level. The second high liquid level sensor 35 and the second low liquid level sensor 34 are installed on the inner wall of the second adsorption box 9. The second high liquid level sensor 35 and the second low liquid level sensor 34 help to control the clean water Liquid level, the side of the first adsorption box 3 is connected with the first liquid discharge pipe 16 and the first liquid inlet pipe 18, the pipe section of the first liquid discharge pipe 16 is installed with the first shut-off valve 17, the pipe section of the first liquid inlet pipe 18 is installed with the second shut-off valve 19, the side of the second adsorption box 9 is connected with the second liquid discharge pipe 29 and the second liquid inlet pipe 27, the pipe section of the second liquid discharge pipe 29 is installed with the third shut-off valve 30, the pipe section of the second liquid inlet pipe 27 is installed with the fourth shut-off valve 28, the pipe section of the air inlet pipe 7 is installed with the gas flow meter 20 and the first solenoid valve 21, the pipe section of the first exhaust pipe 8 is installed with the second solenoid valve 22, and the pipe section of the second exhaust pipe 12 is installed with the fourth solenoid valve 33.
[0027] Reference Figure 4 A microporous atomizing plate 26 is installed in the port of the tee 5 near the pumping mechanism 4, and a guide plate 25 is fixed in the port of the tee 5 near the outlet. The microporous atomizing plate 26 can atomize the alkali solution to facilitate better mixing of the alkali solution and the flue gas, and the guide plate 25 can help mix the alkali solution and the flue gas.
[0028] Working principle: When in use, the first adsorption box 3 is filled with alkaline solution, the second adsorption box 9 is filled with clean water, the flue gas enters the tee 5 through the air inlet pipe 7, the liquid extraction mechanism 4 extracts the alkaline solution and inputs it into the tee 5, in the tee 5, the flue gas and the alkaline solution are mixed, and the primary adsorption treatment of the flue gas is achieved, the residual tail gas enters the main pipe 10 through the first exhaust pipe 8, and then is sent to the unit pipe 11 by the main pipe 10 and discharged from the exhaust hole 31 on the unit pipe 11, the clean water performs secondary adsorption on the flue gas, the residual tail gas enters the cone cover 14 through the second exhaust pipe 12, and then is output from the cone cover 14 and passes through the activated carbon filter The net 27 filters to achieve three adsorptions. Through a total of three adsorption processes, the absorption efficiency is higher, which effectively improves the quality of the remaining exhaust gas, reduces damage to the environment, and is very environmentally friendly. The controller 15 is used to control the electrical part of the entire device for easy management. The first high liquid level sensor 24 and the first low liquid level sensor 23 help to control the alkali liquid level, the second high liquid level sensor 35 and the second low liquid level sensor 34 help to control the clean water level, and the microporous atomizing plate 26 can atomize the alkali liquid to facilitate better mixing of the alkali liquid and the flue gas. The guide plate 25 can help mix the alkali liquid and the flue gas.
[0029] The operating principle of the liquid pumping mechanism 4 is as follows: the liquid pump 41 pumps liquid, sucks alkaline liquid through the spherical mesh cover 43, and then delivers it into the tee 5 through the liquid guide tube 42.
[0030] The above description is only a preferred specific implementation manner of the present invention, but the protection scope of the present invention is not limited thereto. Any technician familiar with the technical field can make equivalent replacements or changes according to the technical scheme and inventive concept of the present invention within the technical scope disclosed by the present invention, which should be covered by the protection scope of the present invention.
Claims
1. A high-efficiency flue gas desulfurization environmental protection device, comprising a first adsorption box (3) and a second adsorption box (9), characterized in that: A tee (5) is fixed inside the first adsorption box (3) via a first bracket (6); a liquid extraction mechanism (4) for inputting liquid into the tee (5) is installed inside the first adsorption box (3); an air inlet pipe (7) for inputting gas into the tee (5) is connected to the tee (5); a first exhaust pipe (8) is connected between the first adsorption box (3) and the second adsorption box (9); the first exhaust pipe (8) is connected to a main pipe (10); the main pipe (10) is connected to a plurality of unit pipes (11); exhaust holes (31) are provided on the unit pipes (11); the second adsorption box (9) is connected to a conical cover (14) via a second exhaust pipe (12); the conical cover (14) is fixed to the second adsorption box (9) via a second bracket (13); an activated carbon filter (27) is installed at the port of the conical cover (14).
2. A high-efficiency flue gas desulfurization environmental protection device according to claim 1, characterized in that: The first adsorption box (3) and the second adsorption box (9) are mounted on a bottom plate (1), and rollers (2) are mounted on the four bottom corners of the bottom plate (1).
3. A high-efficiency flue gas desulfurization environmental protection device according to claim 2, characterized in that: The roller (2) is provided with a brake pad, and the base plate (1) is installed with a controller (15).
4. The high-efficiency flue gas desulfurization environmental protection device according to claim 1 is characterized in that: The liquid extraction mechanism (4) comprises a liquid extraction pump (41), a liquid guide tube (42), and a spherical mesh cover (43); the liquid guide tube (42) is connected to a port of a tee (5); a liquid extraction pump (41) is installed on a pipe section of the liquid guide tube (42); the liquid extraction pump (41) is installed on the inner wall of the first adsorption box (3); and a port of the liquid guide tube (42) is connected to the spherical mesh cover (43).
5. The high-efficiency flue gas desulfurization environmental protection device according to claim 1 is characterized in that: A first high liquid level sensor (24) and a first low liquid level sensor (23) are installed on the inner wall of the first adsorption box (3), and a second high liquid level sensor (35) and a second low liquid level sensor (34) are installed on the inner wall of the second adsorption box (9).
6. The high-efficiency flue gas desulfurization environmental protection device according to claim 1 is characterized in that: The first adsorption box (3) is connected to a first liquid discharge pipe (16) and a first liquid inlet pipe (18) on its side, a first shut-off valve (17) is installed on the pipe section of the first liquid discharge pipe (16), a second shut-off valve (19) is installed on the pipe section of the first liquid inlet pipe (18), the second adsorption box (9) is connected to a second liquid discharge pipe (29) and a second liquid inlet pipe (27) on its side, a third shut-off valve (30) is installed on the pipe section of the second liquid discharge pipe (29), and a fourth shut-off valve (28) is installed on the pipe section of the second liquid inlet pipe (27).
7. The high-efficiency flue gas desulfurization environmental protection device according to claim 1 is characterized in that: A microporous atomizing plate (26) is installed in a port of the tee (5) close to the liquid extraction mechanism (4), and a guide plate (25) is fixed in a port of the tee (5) close to the outlet.
8. The high-efficiency flue gas desulfurization environmental protection device according to claim 1 is characterized in that: A gas flow meter (20) and a first solenoid valve (21) are installed on the pipe section of the air intake pipe (7), a second solenoid valve (22) is installed on the pipe section of the first exhaust pipe (8), and a fourth solenoid valve (33) is installed on the pipe section of the second exhaust pipe (12).