Wet removal device for flue gas pollutants of glass kiln
By designing a wet removal device for flue gas pollutants in the glass kiln, the contact efficiency between the flue gas and the treatment liquid is improved by using the porous plate and the spray assembly, solving the problems of low efficiency and high cost in the traditional method, and achieving efficient and economical pollutant removal effect.
Patent Information
- Application Number
- CN202422491330.7
- Authority / Receiving Office
- CN · China
- Patent Type
- Utility models(China)
- Current Assignee / Owner
- Filing Date
- 2024-10-15
- Publication Date
- 2025-08-08
- Estimated Expiration
- 2034-10-15
AI Technical Summary
Traditional flue gas treatment methods such as dry and semi-dry methods are inefficient, costly and complex in glass kiln flue gas treatment, making it difficult to effectively remove pollutants such as sulfur dioxide, nitrogen oxides and particulate matter.
A wet removal device for flue gas pollutants in glass kilns is designed, including a treatment tank, storage tank, water storage tank, spray assembly, intake pipe, exhaust pipe, water pump and hollow plate. Through the combination of multi-porous plate structure, spray assembly and dehumidification filter plate, effective contact and circulation treatment between the flue gas and the treatment liquid is achieved.
It improves pollutant removal efficiency, is simple in structure and convenient in operation, has significant environmental protection effects and economicality, and reduces environmental pollution.
Smart Images

Figure CN223196786U_ABST
Abstract
Description
Technical Field
[0001] The utility model relates to the technical field of industrial kiln flue gas pollutant treatment, in particular to a device for wet removal of flue gas pollutants from a glass kiln. Background Art
[0002] During the glass production process, the flue gas emitted by glass furnaces contains a large amount of pollutants such as sulfur dioxide, nitrogen oxides, and particulate matter, which pose serious risks to the environment and human health. Traditional flue gas treatment methods include dry and semi-dry removal technologies, but these methods often suffer from low treatment efficiency, high operating costs, and complex equipment.
[0003] Therefore, it is particularly important to develop an efficient, economical and simple-structured wet removal device.
[0004] The information disclosed in this background technology section is only intended to increase the understanding of the overall background of the present invention, and should not be regarded as an admission or any form of suggestion that the information constitutes the prior art already known to those skilled in the art. Utility Model Content
[0005] The purpose of the present invention is to solve the shortcomings mentioned in the above background technology and to propose a wet method for removing pollutants from flue gas of a glass kiln.
[0006] The above technical objectives of the utility model are achieved through the following technical solutions: A device for wet removal of pollutants from flue gas of a glass kiln, comprising a treatment tank, a storage tank, a water storage tank, a spray assembly, an air inlet pipe, an exhaust pipe, a water pump and a hollow plate;
[0007] The air inlet pipe and the exhaust pipe are both fixedly mounted on the treatment tank, a plurality of through holes are opened on the top inner wall of the hollow plate 1 and are arranged in the treatment tank, the air inlet pipe passes through the treatment tank and extends upward from the center position of the bottom of the treatment tank into the treatment tank and is fixedly connected to the hollow plate 1, and the air inlet pipe and the hollow plate 1 remain in a connected state, the storage tank and the water storage tank are respectively fixedly mounted with connecting pipe 1 and connecting pipe 2, and the storage tank and the water storage tank are respectively connected to the treatment tank through connecting pipe 1 and connecting pipe 2, a slag discharge pipe is fixedly mounted on the storage tank, the spray assembly is arranged on the exhaust pipe, one end of the exhaust pipe is rotatably mounted with a shell with an open bottom and connected to the exhaust pipe, the shell is connected to the spray assembly, the water pump is fixedly mounted on the outside of the treatment tank, the water inlet and water outlet of the water pump are respectively fixedly mounted with a water suction pipe and a delivery pipe, and the water suction pipe and the delivery pipe are respectively connected to the water storage tank and the spray assembly.
[0008] Preferably, the spray assembly includes a hollow plate 2 and a plurality of spray heads, the hollow plate 2 is rotatably mounted on the exhaust pipe, and the plurality of spray heads are fixedly mounted on the bottom inner wall of the hollow plate 2.
[0009] Preferably, two porous plates are fixedly installed in the processing tank, and the two porous plates are respectively located on the upper and lower sides of the hollow plate 1, and the connecting pipe 1 and the connecting pipe 2 are respectively located above and below the lower porous plate.
[0010] Preferably, fan blades are fixedly mounted on the inner side wall of the shell.
[0011] Preferably, a dehumidification filter plate arranged in a spherical shape is fixedly mounted on the inner side wall of the shell.
[0012] Preferably, the portion of the exhaust pipe outside the treatment tank is provided with a downward U-shaped bend, a collecting tank is installed on the exhaust pipe with a sealing thread, and the collecting tank is arranged at the lowest point of the U-shaped bend.
[0013] Preferably, a circular opening is opened in the center of the top side of the second hollow plate, one end of the delivery pipe away from the water pump extends into the circular opening, and a sealing ring for movable sealing on the top of the second hollow plate is fixedly installed on the delivery pipe.
[0014] Preferably, a spherical mesh plate adapted to the second connecting pipe is fixedly mounted on the inner side wall of the treatment tank.
[0015] Preferably, the inner wall of the bottom of the processing tank is arranged in a state of being lower on the left and higher on the right, and the connecting pipe 1 is located at the lowest point of the inner wall of the bottom of the processing tank.
[0016] Preferably, a transparent glass tube arranged in an E shape is fixedly mounted on the processing tank, and the two lower ports of the transparent glass tube are respectively located on the upper and lower sides of the porous plate below.
[0017] The beneficial effects of the utility model are:
[0018] The hollow plate 1 with multiple through holes can effectively disperse the flue gas entering the treatment tank, thereby increasing the contact area between the flue gas and the treatment liquid and enhancing the removal efficiency of pollutants. At the same time, the water storage tank and the water storage tank are connected to the treatment tank through connecting pipe 1 and connecting pipe 2, ensuring the recycling of the treatment liquid. In addition, since the inner wall of the bottom of the treatment tank is set to be low on the left and high on the right, and the connection pipe 1 is located at the lowest point of the inner wall of the bottom of the treatment tank, it can ensure that the precipitated debris flows into the storage tank, which is convenient for subsequent cleaning and maintenance. The setting of the spray component can spray the flue gas treated by the treatment liquid in the treatment tank, further improving the removal efficiency of pollutants.
[0019] The setting of the two porous plates can not only slow down the rising speed of the flue gas in the treatment liquid, but also reduce the impact of the flue gas injection into the treatment liquid causing disturbance of the treatment liquid on the sediment in the treatment tank. At the same time, the spherical mesh plate can avoid the influence of solid debris on the second water flow in the connecting pipe.
[0020] By setting the fan blades and dehumidification filter plates in the shell, the hollow plate 2 can be controlled to rotate when the treated flue gas is discharged through the exhaust pipe, thereby realizing rotary spraying, further improving the flue gas treatment efficiency, and dehumidifying the discharged flue gas.
[0021] The U-shaped bend on the exhaust pipe and the setting of the collection tank can further reduce the moisture in the exhaust flue gas and effectively collect it, thereby reducing environmental pollution. The setting of the sealing ring with a movable seal on the top of the hollow plate 2 ensures that the delivery pipe transports the treatment liquid in the water storage tank to the hollow plate 2, while ensuring the normal spraying operation of the sprinkler head. The setting of the transparent glass tube makes it easy to intuitively observe the amount of treatment liquid in the treatment tank, so as to timely adjust the replenishment and discharge of the treatment liquid.
[0022] In summary, the utility model realizes the efficient wet removal of glass kiln flue gas pollutants through a series of structural designs, and has the advantages of simple structure, convenient operation, high treatment efficiency, and significant environmental protection effect. BRIEF DESCRIPTION OF THE DRAWINGS
[0023] In order to more clearly illustrate the technical solutions in the embodiments of the present invention, the following briefly introduces the drawings required for use in the description of the embodiments. Obviously, the drawings described below are only some embodiments of the present invention. For ordinary technicians in this field, other drawings can be obtained based on these drawings without paying any creative work.
[0024] Figure 1 This is a schematic diagram of the three-dimensional structure of a wet-process removal device for glass furnace flue gas pollutants proposed in the utility model;
[0025] Figure 2 This is a schematic cross-sectional view of a device for wet removal of pollutants from flue gas of a glass kiln proposed in the present invention;
[0026] Figure 3 This is a structural schematic diagram of part A of a wet removal device for glass furnace flue gas pollutants proposed in the utility model.
[0027] In the figure: 1. treatment tank; 101. transparent glass tube; 11. air inlet pipe; 12. hollow plate 1; 13. porous plate; 2. storage tank; 21. connecting pipe 1; 22. slag discharge pipe; 3. water storage tank; 31. connecting pipe 2; 311. spherical mesh plate; 4. exhaust pipe; 401. collecting tank; 41. shell; 42. fan blade; 43. dehumidification filter plate; 5. hollow plate 2; 51. water pump; 52. suction pipe; 53. delivery pipe; 54. sealing ring. DETAILED DESCRIPTION
[0028] The following will clearly and completely describe the technical solutions of the present invention in conjunction with specific embodiments. Obviously, the embodiments described are only some of the embodiments of the present invention, and not all of them. All other embodiments derived by persons of ordinary skill in the art based on the embodiments of the present invention without inventive effort are also within the scope of protection of the present invention.
[0029] Reference Figure 1-3, a wet method for removing pollutants from flue gas of a glass kiln, comprising a treatment tank 1, a storage tank 2, a water storage tank 3, an air intake pipe 11, an exhaust pipe 4, a water pump 51 and a hollow plate 12, the air intake pipe 11 and the exhaust pipe 4 are both fixedly mounted on the treatment tank 1, a plurality of through holes are provided on the top inner wall of the hollow plate 12 and are arranged in the treatment tank 1, the air intake pipe 11 passes through the treatment tank 1 and extends upward from the center position of the bottom of the treatment tank 1 into the treatment tank 1 and is fixedly connected to the hollow plate 12, and the air intake pipe 11 and the hollow plate 12 are kept in communication, which can achieve the purpose of controlling the air intake to a certain extent. The pipe 11 is injected into the treatment tank 1 for preliminary cooling of the flue gas to be treated. The storage tank 2 and the water tank 3 are respectively fixedly installed with a connecting pipe 1 21 and a connecting pipe 2 31, and the storage tank 2 and the water tank 3 are connected to the treatment tank 1 through the connecting pipe 1 21 and the connecting pipe 2 31, respectively. A slag discharge pipe 22 is fixedly installed on the storage tank 2, and a hollow plate 2 5 is rotatably installed on the exhaust pipe 4. A plurality of spray heads are fixedly installed on the inner wall of the bottom side of the hollow plate 2 5, which can spray the flue gas floating in the treatment liquid below. One end of the exhaust pipe 4 is rotatably installed with a bottom opening and connected to the exhaust pipe 4. The shell 41 is connected to the hollow plate 2 5, and the water pump 51 is fixedly installed on the outside of the treatment tank 1. The water inlet and outlet of the water pump 51 are respectively fixedly installed with a water pumping pipe 52 and a delivery pipe 53, and the water pumping pipe 52 is connected to the water storage tank 3. A circular opening is opened in the center of the top side of the hollow plate 2 5, and the delivery pipe 53 extends into the circular opening at one end away from the water pump 51. A sealing ring 54 for movable sealing at the top of the hollow plate 2 5 is fixedly installed on the delivery pipe 53, which can ensure that the delivery pipe 53 delivers the treatment liquid in the water storage tank 3 to the hollow plate 2 5, and at the same time can ensure that the spray head During normal spraying operation, two porous plates 13 are fixedly installed in the treatment tank 1. The two porous plates 13 are respectively located on the upper and lower sides of the hollow plate 12, and the connecting pipe 1 21 and the connecting pipe 2 31 are respectively located above and below the lower porous plate 13. The upper porous plate 13 can slow down the rising speed of the flue gas in the treatment liquid, and the porous plate 13 arranged at the bottom can reduce the impact of the flue gas on the sediment in the treatment tank 1 when it is injected into the treatment liquid without affecting the downward sedimentation of the solid sediment, and at the same time, it can prevent the residual solid debris on the lower porous plate 13 from submerging the connecting pipe 2 31.
[0030] In this embodiment, in order to obtain a rotational driving force for the hollow plate 2 5 and enable the multiple spray heads on the hollow plate 2 5 to re-treat the flue gas emerging from the treatment liquid by a rotary spraying method, fan blades 42 are fixedly installed on the inner wall of the shell 41.
[0031] In this embodiment, in order to intercept and filter the moisture in the exhaust pipe 4 when exhausting the gas, a dehumidification filter plate 43 with a spherical surface is fixedly mounted on the inner wall of the shell 41 .
[0032] In this embodiment, in order to further reduce the moisture in the exhaust flue gas and effectively collect the moisture, the part of the exhaust pipe 4 located outside the treatment tank 1 is provided with a downward U-shaped bend, and a collection tank 401 is installed on the exhaust pipe 4 with a sealing thread, and the collection tank 401 is set at the lowest point of the U-shaped bend.
[0033] In this embodiment, in order to prevent solid debris from entering the water storage tank 3 through the second connecting pipe 31 and at the same time not affect the backflow of the treated liquid into the water storage tank 3, a spherical mesh plate 311 adapted to the second connecting pipe 31 is fixedly installed on the inner wall of the treatment tank 1.
[0034] In this embodiment, in order to ensure that the settled debris flows into the storage tank 2 by itself, the bottom inner wall of the processing tank 1 is set to be low on the left and high on the right, and the connecting pipe 21 is located at the lowest point of the bottom inner wall of the processing tank 1.
[0035] In this embodiment, in order to facilitate intuitive observation of the amount of treatment liquid in the treatment tank 1, a transparent glass tube 101 arranged in an E shape is fixedly installed on the treatment tank 1, and the two lower ports of the transparent glass tube 101 are respectively located on the upper and lower sides of the porous plate 13 below.
[0036] Working principle: When in use, first turn on the power and inject an appropriate amount of treatment liquid into the water storage tank 3, then keep the treatment tank 1 connected with the glass kiln flue gas exhaust port through the air inlet pipe 11 and start the water pump 51. The treatment liquid in the water storage tank 3 is sucked into the water pump 51 through the suction pipe 52, and then transported to the hollow plate 2 5 through the delivery pipe 53, and then evenly sprayed into the treatment tank 1 through the multiple spray heads on the hollow plate 2 5. When the air inlet pipe 11 introduces the flue gas generated by the glass kiln into the treatment tank 1, the flue gas is first implanted into the treatment liquid through the multiple through holes of the hollow plate 12 for treatment.
[0037] The flue gas comes into contact with the treatment liquid in the treatment tank 1, and the pollutants therein are absorbed or adsorbed by the treatment liquid to achieve wet removal. Since two porous plates 13 are installed in the treatment tank 1, the flue gas will be delayed by the upper porous plate 13 during the rising process, causing the floating speed to be slowed down, thereby increasing the contact time with the treatment liquid and thus improving the removal efficiency. At the same time, the lower porous plate 13 can also prevent the solid precipitate from sinking to the bottom inner wall of the treatment tank 1 and being affected by the treatment liquid disturbed by the flue gas, thereby ensuring the stable sedimentation of the precipitate.
[0038] The treated flue gas continues to rise and is further sprayed through the spray head of the hollow plate 2 5 to ensure that the residual pollutants in the flue gas are completely removed. The treated flue gas then enters the exhaust pipe 4, and the fan blades 42 in the shell 41 drive the hollow plate 2 5 to rotate, realizing rotary spraying and further improving the treatment effect.
[0039] In the exhaust pipe 4, the dehumidification filter plate 43 intercepts and filters out most of the moisture in the flue gas, reducing moisture emissions. At the same time, due to the U-shaped bend design on the exhaust pipe 4, the moisture in the flue gas will condense here and flow into the collection tank 401, realizing effective collection of moisture.
[0040] The spherical mesh plate 311 at the bottom of the treatment tank 1 is set to prevent solid debris from entering the water storage tank 3, while allowing the treatment liquid to flow back freely. The precipitated debris will naturally flow into the storage tank 2 due to the inclined design of the bottom of the treatment tank 1, which is convenient for subsequent cleaning and treatment. The transparent glass tube 101 is set so that the operator can intuitively observe the water level of the treatment liquid in the treatment tank 1, ensuring the normal operation of the entire device, realizing the effective removal of pollutants in the glass kiln flue gas, and achieving the goals of environmental protection and energy saving.
[0041] The above describes in detail the wet-process removal device for glass furnace flue gas pollutants provided by the present invention. This article uses specific examples to illustrate the principles and implementation methods of the present invention. The description of the above examples is only intended to help understand the method and core concept of the present invention. It should be noted that those skilled in the art can make various improvements and modifications to the present invention without departing from the principles of the present invention, and such improvements and modifications also fall within the scope of protection of the claims of the present invention.
Claims
1. A device for wet removal of pollutants from flue gas of a glass furnace, characterized in that: It includes a processing tank (1), a storage tank (2), a water storage tank (3), a spray assembly, an air inlet pipe (11), an exhaust pipe (4), a water pump (51) and a hollow plate (12); The air intake pipe (11) and the exhaust pipe (4) are both fixedly mounted on the treatment tank (1); a plurality of through holes are provided on the top inner wall of the hollow plate (12) and are arranged in the treatment tank (1); the air intake pipe (11) passes through the treatment tank (1) and extends upward from the center of the bottom of the treatment tank (1) into the treatment tank (1) and is fixedly connected to the hollow plate (12); the air intake pipe (11) and the hollow plate (12) are kept in a connected state; the storage tank (2) and the water tank (3) are respectively fixedly mounted with a connecting pipe (21) and a connecting pipe (31); and the storage tank (2) and the water tank (3) are respectively connected through the connecting pipe (21) ) and a connecting pipe (31) are connected to the processing tank (1); a slag discharge pipe (22) is fixedly installed on the storage tank (2); the spray assembly is arranged on the exhaust pipe (4); one end of the exhaust pipe (4) is rotatably mounted with a shell (41) with an open bottom and connected to the exhaust pipe (4); the shell (41) is connected to the spray assembly; the water pump (51) is fixedly mounted on the outside of the processing tank (1); a water inlet and a water outlet of the water pump (51) are respectively fixedly mounted with a water pumping pipe (52) and a delivery pipe (53); and the water pumping pipe (52) and the delivery pipe (53) are respectively connected to the water storage tank (3) and the spray assembly.
2. The device for wet removal of pollutants from flue gas of a glass furnace according to claim 1, characterized in that: The spray assembly comprises a second hollow plate (5) and a plurality of spray heads. The second hollow plate (5) is rotatably mounted on the exhaust pipe (4), and the plurality of spray heads are fixedly mounted on the inner wall of the bottom side of the second hollow plate (5).
3. The device for wet removal of pollutants from glass furnace flue gas according to claim 1, characterized in that: Two porous plates (13) are fixedly installed in the processing tank (1), and the two porous plates (13) are respectively located on the upper and lower sides of the hollow plate (12), and the connecting pipe (21) and the connecting pipe (31) are respectively located above and below the lower porous plate (13).
4. The device for wet removal of pollutants from glass furnace flue gas according to claim 1, characterized in that: A fan blade (42) is fixedly mounted on the inner side wall of the housing (41).
5. The device for wet removal of pollutants from flue gas of a glass furnace according to claim 1, characterized in that: A dehumidification filter plate (43) arranged in a spherical shape is fixedly mounted on the inner side wall of the housing (41).
6. The device for wet removal of pollutants from flue gas of a glass furnace according to claim 1, characterized in that: The portion of the exhaust pipe (4) located outside the treatment tank (1) is provided with a downward U-shaped bend, and a collecting tank (401) is installed on the exhaust pipe (4) in a sealing thread, and the collecting tank (401) is arranged at the lowest point of the U-shaped bend.
7. The device for wet removal of pollutants from flue gas of a glass furnace according to claim 2, characterized in that: A circular opening is provided at the center of the top side of the second hollow plate (5), and one end of the delivery pipe (53) away from the water pump (51) extends into the circular opening, and a sealing ring (54) for movable sealing of the top of the second hollow plate (5) is fixedly mounted on the delivery pipe (53).
8. The device for wet removal of pollutants from flue gas of a glass furnace according to claim 1, characterized in that: A spherical mesh plate (311) adapted to the second connecting pipe (31) is fixedly mounted on the inner side wall of the processing tank (1).
9. The device for wet removal of pollutants from flue gas of a glass furnace according to claim 1, characterized in that: The bottom inner wall of the processing tank (1) is arranged in a state where the left side is lower and the right side is higher, and the connecting pipe (21) is located at the lowest point of the bottom inner wall of the processing tank (1).
10. The device for wet removal of pollutants from flue gas of a glass furnace according to claim 3, characterized in that: A transparent glass tube (101) arranged in an E-shape is fixedly mounted on the processing tank (1), and the two lower ports of the transparent glass tube (101) are respectively located on the upper and lower sides of the porous plate (13) below.