Glass kiln flue gas treatment device

Abstract

The utility model provides a glass kiln flue gas treatment device which comprises a gas inlet pipeline, the first end of the gas inlet pipeline communicates with a gas outlet of a glass kiln flue, and the second end of the gas inlet pipeline is provided with a first branch, a second branch and a third branch; the first dust removal pipeline assembly is communicated with the first branch, the first dust removal pipeline assembly is communicated with exhaust equipment, and a first valve is arranged on the first dust removal pipeline assembly; the second dust removal pipeline assembly is communicated with the second branch, the second dust removal pipeline assembly is communicated with the exhaust equipment, and a second valve is arranged on the second dust removal pipeline assembly; and the standby pipeline is communicated with the third branch, the standby pipeline is communicated with the exhaust equipment, and a third valve is arranged on the standby pipeline. According to the technical scheme, the problem of low waste gas treatment efficiency caused by the fact that a gas path is blocked by boride in the flue gas dust removal process of the medium borosilicate glass kiln in the prior art is effectively solved.

Description

Technical Field

[0001] The present application relates to the technical field of waste gas treatment, and in particular to a glass kiln flue gas treatment device. Background Art

[0002] Medium borosilicate glass has good solubility and acid and alkali resistance, so it is often used in the medical industry, such as storing medicines.

[0003] Generally, a large amount of high-temperature flue gas is generated during the production process of medium-bay silicon glass. When treating the flue gas, it is necessary to cool the flue gas and purify it so that it meets the emission standards before being discharged.

[0004] In the flue gas treatment device of the prior art, the flue gas after cooling produces a large amount of boride crystals. The boride crystals easily adhere to the inner wall of the flue gas path and block the flue gas path. Therefore, the flue gas treatment device needs to be cleaned frequently, and the working efficiency is low, such as CN204159174U. Utility Model Content

[0005] A technical problem to be solved by the present application is that, during the dust removal process of the flue gas of the medium-borosilicate glass furnace, there is a problem of low waste gas treatment efficiency due to the blockage of the gas path by borides.

[0006] In order to solve the above technical problems, the present application provides a glass kiln flue gas treatment device.

[0007] According to the present application, a glass kiln flue gas treatment device includes: an air intake pipeline, the first end of the air intake pipeline is connected to the air outlet of the glass kiln flue, and the second end of the air intake pipeline has a first branch, a second branch and a third branch; a first dust removal pipeline assembly, the first dust removal pipeline assembly is connected to the first branch, the first dust removal pipeline assembly is connected to the exhaust equipment, and the first dust removal pipeline assembly is provided with a first valve; a second dust removal pipeline assembly, the second dust removal pipeline assembly is connected to the second branch, the second dust removal pipeline assembly is connected to the exhaust equipment, and the second dust removal pipeline assembly is provided with a second valve; a spare pipeline, the spare pipeline is connected to the third branch, the spare pipeline is connected to the exhaust equipment, and the spare pipeline is provided with a third valve.

[0008] In some embodiments, the first dust removal pipeline assembly includes a first dust removal pipeline, a first cyclone dust removal structure, a first cooling structure and a first bag dust collection structure. The first end of the first dust removal pipeline is connected to the first branch, and the first cyclone dust collection structure, the first cooling structure and the first bag dust collection structure are arranged in sequence from the first end of the first dust collection pipeline to the second end of the first dust collection pipeline.

[0009] In some embodiments, the second dust removal pipeline assembly includes a second dust removal pipeline, a second cyclone dust removal structure, a second cooling structure and a second bag dust removal structure. The first end of the second dust removal pipeline is connected to the second branch, and the second cyclone dust removal structure, the second cooling structure and the second bag dust removal structure are arranged in sequence from the first end of the second dust collection pipeline to the second end of the second dust collection pipeline.

[0010] In some embodiments, the first cyclone dust removal structure includes a first air inlet, a first air outlet, a first dust removal bin and a first feed pipeline, the first air inlet is connected to the first dust removal bin, the first air outlet is connected to the first dust removal bin, the first end of the first feed pipeline is connected to the first dust removal bin, and the second end of the first feed pipeline is connected to the quicklime discharge device.

[0011] In some embodiments, the second cyclone dust removal structure includes a second air inlet, a second air outlet, a second dust removal bin and a second feed pipeline, the second air inlet is connected to the second dust removal bin, the second air outlet is connected to the second dust removal bin, the first end of the second feed pipeline is connected to the second dust removal bin, and the second end of the second feed pipeline is connected to the quicklime discharge device.

[0012] In some embodiments, the first end of the spare pipeline is connected to the third branch, the second end of the spare pipeline includes a fourth branch and a fifth branch, the fourth branch is connected to the first dust removal pipeline, and a fourth valve is provided on the fourth branch, the fifth branch is connected to the second dust removal pipeline, and a fifth valve is provided on the fifth branch.

[0013] In some embodiments, the first dust removal pipeline assembly also includes a sixth branch, the first end of the sixth branch is located between the first cyclone dust removal structure and the first cooling structure and is connected to the first dust removal pipeline, the second end of the sixth branch is located between the second cyclone dust removal structure and the second cooling structure and is connected to the second dust removal pipeline, and a sixth valve is provided on the sixth branch.

[0014] In some embodiments, the first dust removal pipeline assembly also includes a seventh branch, the first end of the seventh branch is located between the first cooling structure and the first bag dust removal structure and is connected to the first dust removal pipeline, the second end of the seventh branch is located between the second cooling structure and the second bag dust removal structure and is connected to the second dust removal pipeline, and a seventh valve is provided on the seventh branch.

[0015] In some embodiments, the first dust removal pipeline assembly also includes an eighth branch, the first end of the eighth branch is located between the first bag dust removal structure and the exhaust equipment and is connected to the first dust collection pipeline, the second end of the eighth branch is located between the second bag dust removal structure and the exhaust equipment and is connected to the second dust collection pipeline, and an eighth valve is provided on the eighth branch.

[0016] In some embodiments, the first dust removal pipeline assembly also includes a first induced draft fan, which is arranged on the first dust removal pipeline and is located on the side of the first bag dust removal structure close to the second end of the first dust removal pipeline.

[0017] Through the above technical solution, the glass kiln flue gas treatment device provided by the present application, the kiln exhaust gas enters the air intake pipe, the first valve is opened, the second valve and the third valve are closed, the flue gas passes through the first dust removal pipeline assembly for dust removal, if the first dust removal pipeline assembly is blocked by borides or fails, the first valve and the third valve are closed, the second valve is opened, and the flue gas passes through the second dust removal pipeline assembly for dust removal. The first dust removal pipeline assembly and the second dust removal pipeline assembly are used alternately, which is convenient for the staff to clean the two in time to avoid blockage, and the entire device can still complete dust removal while the cleaning process is in progress. If both the first dust removal pipeline assembly and the second dust removal pipeline assembly cannot be used, the first valve and the second valve are closed, the third valve is opened, and the flue gas is passed into the exhaust equipment from the spare pipeline. The technical solution of the present application effectively solves the problem of low exhaust gas treatment efficiency caused by boride blocking the gas path in the dust removal process of the medium borosilicate glass kiln flue gas in the prior art. BRIEF DESCRIPTION OF THE DRAWINGS

[0018] In order to more clearly illustrate the embodiments of the present application or the technical solutions in the prior art, the following briefly introduces the drawings required for use in the embodiments or the description of the prior art. Obviously, the drawings described below are only some embodiments of the present application. For ordinary technicians in this field, other drawings can be obtained based on these drawings without any creative work.

[0019] Figure 1 The figure shows a structural diagram of a glass furnace fume treatment device disclosed in the first embodiment of the present application;

[0020] Figure 2 Shown Figure 1 A schematic structural diagram of a first cyclone dust removal structure of a glass furnace flue gas treatment device;

[0021] Figure 3 Shown Figure 1 A structural schematic diagram of a first cooling structure of a glass furnace flue gas treatment device;

[0022] Figure 4 Shown Figure 1 A schematic structural diagram of a first bag-type dust removal structure of a glass furnace flue gas treatment device;

[0023] Figure 5 Shown Figure 1 A schematic structural diagram of a second cyclone dust removal structure of a glass furnace flue gas treatment device;

[0024] Figure 6 A structural schematic diagram of a glass kiln fume treatment device disclosed in Example 2 of the present application is shown.

[0025] Description of reference numerals:

[0026] 10. Air intake pipeline; 11. First branch; 12. Second branch; 13. Third branch; 20. First dust removal pipeline assembly; 21. First dust removal pipeline; 22. First cyclone dust removal structure; 221. First air inlet; 222. First air outlet; 223. First dust removal bin; 224. First feeding pipeline; 23. First cooling structure; 24. First bag-type dust removal structure; 25. Sixth branch; 26. Seventh branch; 27. Eighth branch; 28. First induced draft fan; 30. Second dust removal pipeline assembly; 31. Second dust removal pipeline; 32. Second cyclone dust removal structure; 321. Second air inlet; 322. Second air outlet; 323. Second dust removal bin; 324. Second feeding pipeline; 33. Second cooling structure; 34. Second bag-type dust removal structure; 35. Second induced draft fan; 40. Spare pipeline; 41. Fourth branch; 42. Fifth branch. DETAILED DESCRIPTION

[0027] The following detailed description of the embodiments of the present application is provided in conjunction with the accompanying drawings and examples. The detailed description of the following examples and the accompanying drawings are intended to illustrate the principles of the present application, but are not intended to limit the scope of the present application. The present application may be implemented in many different forms and is not limited to the specific embodiments disclosed herein, but rather encompasses all technical solutions within the scope of the claims.

[0028] The present application provides these embodiments to make this application thorough and complete, and to fully express the scope of this application to those skilled in the art. It should be noted that: unless otherwise specifically stated, the relative arrangement of parts and steps, the composition of materials, numerical expressions and numerical values ​​set forth in these embodiments should be interpreted as merely exemplary, and not as limiting.

[0029] It should be noted that, in the description of this application, unless otherwise specified, "plurality" means greater than or equal to two; the terms "upper," "lower," "left," "right," "inner," "outer," and the like, indicating directions or positional relationships, are intended solely to facilitate the description of this application and simplify the description, and do not indicate or imply that the devices or components referred to must have a specific orientation, be constructed, or operate in a specific orientation. Therefore, they should not be construed as limitations on this application. When the absolute position of the object being described changes, the relative positional relationship may also change accordingly.

[0030] In addition, the terms "first," "second," and similar terms used in this application do not denote any order, quantity, or importance, but are simply used to distinguish different parts. "Perpendicular" does not mean perpendicular in the strict sense, but rather means within the tolerance range. "Parallel" does not mean parallel in the strict sense, but rather means within the tolerance range. "Include" or "comprising" and similar terms mean that the elements preceding the word include the elements listed after the word, and do not exclude the possibility of other elements being included.

[0031] It should also be noted that, in the description of this application, unless otherwise expressly specified or limited, the terms "installed," "connected," and "connected" should be understood in a broad sense. For example, they can refer to fixed connections, detachable connections, or integral connections; they can refer to direct connections or indirect connections through an intermediary. A person of ordinary skill in the art will understand the specific meanings of the above terms in this application depending on the specific circumstances. When a specific device is described as being located between a first device and a second device, there may or may not be an intervening device between the specific device and the first or second device.

[0032] All terms used in this application have the same meaning as understood by one of ordinary skill in the art to which this application belongs, unless otherwise specifically defined. It should also be understood that terms defined in, for example, common dictionaries should be interpreted as having a meaning consistent with their meaning in the context of the relevant technology and should not be interpreted in an idealized or highly formal sense, unless explicitly defined as such herein.

[0033] Technologies, methods, and equipment known to ordinary technicians in the relevant art may not be discussed in detail, but where appropriate, the technologies, methods, and equipment should be considered part of the specification.

[0034] like Figures 1 to 5 As shown, the glass kiln flue gas treatment device disclosed in Example 1 of the present application includes: an air intake pipe 10, a first dust removal pipe assembly 20, a second dust removal pipe assembly 30 and a spare assembly. The first end of the air intake pipe 10 is connected to the air outlet of the glass kiln flue, and the second end of the air intake pipe 10 has a first branch 11, a second branch 12 and a third branch 13. The first dust removal pipe assembly 20 is connected to the first branch 11, and the first dust removal pipe assembly 20 is connected to the exhaust equipment. A first valve is provided on the first dust removal pipe assembly 20, and the second dust removal pipe assembly 30 is connected to the second branch 12. The second dust removal pipe assembly 30 is connected to the exhaust equipment. A second valve is provided on the second dust removal pipe assembly 30, and a spare pipe 40 is connected to the third branch 13. The spare pipe 40 is connected to the exhaust equipment, and a third valve is provided on the spare pipe 40.

[0035] Applying the technical solution of Example 1, the kiln exhaust gas enters the air intake pipe 10, the first valve is opened, the second valve and the third valve are closed, and the flue gas passes through the first dust removal pipe assembly 20 for dust removal. If the first dust removal pipe assembly 20 is blocked by borides or fails, the first valve and the third valve are closed, the second valve is opened, and the flue gas passes through the second dust removal pipe assembly 30 for dust removal. The first dust removal pipe assembly 20 and the second dust removal pipe assembly 30 are used alternately, which is convenient for the staff to clean them in time to avoid blockage, and the entire device can still complete dust removal while the cleaning process is in progress. If both the first dust removal pipe assembly 20 and the second dust removal pipe assembly 30 cannot be used, the first valve and the second valve are closed, the third valve is opened, and the flue gas is passed into the exhaust equipment from the spare pipe 40. The technical solution of Example 1 effectively solves the problem of low exhaust gas treatment efficiency caused by boron compounds blocking the gas path during the dust removal process of the flue gas of the medium borosilicate glass kiln in the prior art.

[0036] like Figures 1 to 4 As shown, in the technical solution of Example 1, the first dust removal pipeline assembly 20 includes a first dust removal pipeline 21, a first cyclone dust removal structure 22, a first cooling structure 23, and a first bag dust removal structure 24. The first end of the first dust removal pipeline 21 is connected to the first branch 11, and the first cyclone dust removal structure 22, the first cooling structure 23, and the first bag dust removal structure 24 are arranged in sequence from the first end of the first dust removal pipeline 21 to the second end of the first dust removal pipeline 21. When the flue gas enters the air intake pipeline 10, the first valve is opened, and the second and third valves are closed, the flue gas flows from the first branch 11 into the first dust removal pipeline 21 and passes through the first cyclone dust removal structure 22, the first cooling structure 23, and the first bag dust removal structure 24 in sequence. The first cyclone dust removal structure 22 uses centrifugal force to remove larger and heavier particles from the flue gas. The first cooling structure 23 cools the flue gas to 110°C, causing some boride in the flue gas to crystallize. The flue gas then passes into the first bag dust removal structure 24 for dust removal. The boride particles are trapped by the bags and adhere to the bag surfaces. Clean gas is then discharged from the first bag dust removal structure 24. The first cyclone dust removal structure 22, the first cooling structure 23, and the first bag dust removal structure 24 work together to remove boride particles from the flue gas, ensuring that the exhaust gas meets emission standards and reduces environmental pollution.

[0037] like Figure 1 and Figure 5As shown, in the technical solution of Example 1, the second dust removal pipeline assembly 30 includes a second dust removal pipeline 31, a second cyclone dust removal structure 32, a second cooling structure 33, and a second bag dust removal structure 34. The first end of the second dust removal pipeline 31 is connected to the second branch 12, and the second cyclone dust removal structure 32, the second cooling structure 33, and the second bag dust removal structure 34 are arranged in sequence from the first end of the second dust removal pipeline 31 to the second end of the second dust removal pipeline 31. When the first dust removal pipeline assembly 20 is blocked, the first valve is closed and the second valve is opened, and the flue gas is passed into the second dust removal pipeline assembly 30 and passes through the second cyclone dust removal structure 32, the second cooling structure 33, and the second bag dust removal structure 34 in sequence. The second cyclone dust removal structure 32 uses centrifugal force to remove larger and heavier particles from the flue gas. The second cooling structure 33 cools the flue gas to 110°C. Some of the boride in the flue gas crystallizes and then passes into the second bag dust removal structure 34 for dust removal. The boride particles are blocked by the bag and adhere to the surface of the bag. Clean gas is discharged from the second bag dust removal structure 34. The second cyclone dust removal structure 32, the second cooling structure 33 and the second bag dust removal structure 34 work together to remove the boride particles in the flue gas, so that the exhaust gas meets the emission standards and reduces environmental pollution. When the first dust removal pipeline assembly 20 is activated, the second dust removal pipeline assembly 30 is cleaned to prevent it from being blocked. The second dust removal pipeline assembly 30 is used alternately with the first dust removal pipeline assembly 20 to achieve continuous dust removal of the flue gas and improve dust removal efficiency.

[0038] like Figure 2As shown, in the technical solution of Example 1, the first cyclone dust removal structure 22 includes a first air inlet 221, a first air outlet 222, a first dust removal bin 223 and a first feed pipeline 224, the first air inlet 221 is connected to the first dust removal bin 223, the first air outlet 222 is connected to the first dust removal bin 223, the first end of the first feed pipeline 224 is connected to the first dust removal bin 223, and the second end of the first feed pipeline 224 is connected to the quicklime discharge device. The first dust removal bin 223 includes a conical section and a cylindrical section, the cylindrical section is connected to the conical section, and the first air outlet 222 is arranged on the cylindrical section. The first air outlet has a predetermined angle with the horizontal direction. The exhaust gas enters from the first air outlet 222 and flows downward along the inner wall of the first dust removal bin 223 to form a conical spiral gas. Under the action of centrifugal force, the particles in the gas collide with the inner wall of the first dust removal bin 223, and the particle speed is reduced and falls to the bottom of the first dust removal bin 223 along the inner wall of the first dust removal bin 223 under the action of gravity. A conical guide structure is provided at the bottom of the first dust removal bin 223, and there is a gap between the conical guide structure and the inner wall of the first dust removal bin 223. The solid particles fall from the gap into the recovery box arranged below the first dust removal bin 223. After the gas hits the upper surface of the conical guide structure, it moves upward and is discharged from the first air outlet 222 above. Quicklime slurry is introduced from the first feed line 224 into the first dust removal bin 223. Sulfides and other substances in the exhaust gas react with the quicklime slurry to achieve exhaust gas desulfurization. The reacted quicklime, under the action of centrifugal force, falls into the recovery bin along with the solid particles. The first feed line 224 includes multiple discharge ports, which are evenly arranged and have a diameter of less than 2 mm. This structure ensures that the quicklime ejected from the first feed line 224 is evenly distributed, making the desulfurization reaction more thorough. Furthermore, smaller quicklime slurry droplets are more susceptible to the influence of centrifugal force, which is conducive to the smooth operation of the first cyclone dust removal structure 22.

[0039] like Figure 5 As shown, in the technical solution of Example 1, the second cyclone dust removal structure 32 includes a second air inlet 321, a second air outlet 322, a second dust removal bin 323, and a second feed line 324. The second air inlet 321 is connected to the second dust removal bin 323, the second air outlet 322 is connected to the second dust removal bin 323, the first end of the second feed line 324 is connected to the second dust removal bin 323, and the second end of the second feed line 324 is connected to the quicklime discharge device. The second cyclone dust removal structure 32 shares the same structural principles as the first cyclone dust removal structure 22. The second cyclone dust removal structure 32 can also remove and desulfurize large particulate impurities in the exhaust gas, further reducing residual pollutants in the exhaust gas.

[0040] like Figure 1As shown, in the technical solution of Example 1, the first end of the standby pipeline 40 is connected to the third branch 13, and the second end of the standby pipeline 40 includes a fourth branch 41 and a fifth branch 42. The fourth branch 41 is connected to the first dust removal pipeline 21, and a fourth valve is provided on the fourth branch 41. The fifth branch 42 is connected to the second dust removal pipeline 31, and a fifth valve is provided on the fifth branch 42. The fourth branch 41 is provided on the side of the first bag dust removal structure 24 away from the first cooling structure 23, and the fifth branch 42 is provided on the side of the second bag dust removal structure 34 away from the second cooling structure 33. When both the first dust removal pipeline assembly 20 and the second dust removal pipeline assembly 30 are in an unusable state, the first valve and the second valve are closed, and the third valve is opened, and the smoke is discharged directly from the standby pipeline 40 and eventually enters the exhaust structure. In the actual production process, it is almost impossible that both the first dust removal pipeline assembly 20 and the second dust removal pipeline assembly 30 cannot be used. The setting of the backup pipeline 40 is only used in an emergency in extreme situations to avoid excessive exhaust gas in the glass kiln that is not discharged and causes excessive air pressure in the kiln. When the backup pipeline 40 is needed, the production of the glass kiln should be stopped in time to reduce the phenomenon of untreated exhaust gas being directly discharged into the atmosphere.

[0041] like Figure 1 As shown, in the technical solution of Example 1, the first dust collection pipeline assembly 20 also includes a first induced draft fan 28, which is arranged on the first dust collection pipeline 21 and is located on the side of the first bag-type dust collection structure 24 close to the second end of the first dust collection pipeline 21. The second dust collection pipeline assembly 30 also includes a second induced draft fan 35, which is arranged on the second dust collection pipeline 31 and is located on the side of the second bag-type dust collection structure 34 close to the second end of the second dust collection pipeline 31. The treated flue gas is directly introduced into the chimney by the first induced draft fan 28 and the second induced draft fan 35 and discharged into the atmosphere. The arrangement of the first induced draft fan 28 and the second induced draft fan 35 can effectively reduce the occurrence of turbulence in the gas path.

[0042] like Figure 6As shown, the difference between the technical solution of the second embodiment and the technical solution of the first embodiment is that the first dust removal pipeline assembly 20 further includes a sixth branch 25. The first end of the sixth branch 25 is located between the first cyclone dust removal structure 22 and the first cooling structure 23 and is connected to the first dust removal pipeline 21. The second end of the sixth branch 25 is located between the second cyclone dust removal structure 32 and the second cooling structure 33 and is connected to the second dust removal pipeline 31. A sixth valve is provided on the sixth branch 25. When the first cyclone dust removal structure 22 is not faulty, but the first cooling structure 23 or the first bag dust removal structure 24 is faulty, the sixth valve can be opened and the air inlet of the first cooling structure 23 can be closed, so that the flue gas flows through the first cyclone dust removal structure 22, the second cooling structure 33 and the second bag dust removal structure 34 for dust removal. The provision of the sixth branch 25 and the sixth valve further reduces the number of times the backup pipeline 40 is used.

[0043] like Figure 6 As shown, in the technical solution of Example 2, the first dust removal pipeline assembly 20 also includes a seventh branch 26. The first end of the seventh branch 26 is located between the first cooling structure 23 and the first bag dust removal structure 24 and is connected to the first dust removal pipeline 21. The second end of the seventh branch 26 is located between the second cooling structure 33 and the second bag dust removal structure 34 and is connected to the second dust removal pipeline 31. A seventh valve is provided on the seventh branch 26. The provision of the seventh branch 26 enables airflow to flow through the first cyclone dust removal structure 22, the first cooling structure 23, and the second bag dust removal structure 34 for dust removal. The provision of the seventh branch 26 and the seventh valve further reduces the number of times the spare pipeline 40 is used.

[0044] like Figure 6 As shown, in the technical solution of Example 2, the first dust removal pipeline assembly 20 further includes an eighth branch 27. The first end of the eighth branch 27 is located between the first bag-type dust removal structure 24 and the exhaust device and is connected to the first dust removal pipeline 21. The second end of the eighth branch 27 is located between the second bag-type dust removal structure 34 and the exhaust device and is connected to the second dust removal pipeline 31. An eighth valve is provided on the eighth branch 27. The provision of the eighth branch 27 allows airflow to flow out of the first induced draft fan 28 or the second induced draft fan 35, avoiding the problem of airflow not being able to flow out normally due to a failure of the first induced draft fan 28 or the second induced draft fan 35.

[0045] The technical solution of Example 2 increases the number of gas path options by providing the sixth branch 25, the seventh branch 26, and the eighth branch 27. It allows users to arbitrarily select either the first cyclone dust removal structure 22 or the second cyclone dust removal structure 32 for removing large-particle impurities, the first cooling structure 23 or the second cooling structure 33 for cooling crystallization, the first bag dust removal structure 24 or the second bag dust removal structure 34 for removing small-particle impurities, and the first induced draft fan 28 or the second induced draft fan 35 for gas exhaust. This further avoids the problem of gas needing to be exhausted through the backup pipeline 40 due to equipment failure in both the first dust removal pipeline assembly 20 and the second dust removal pipeline assembly 30, thereby reducing environmental pollution.

[0046] From the above, it can be seen that the technical solution adopted in this application is composed of a cyclone dust collector (a first cyclone dust removal structure 22 and a second cyclone dust removal structure 32), a multi-tube heat exchanger (a first cooling structure 23 and a second cooling structure 33), a bag dust collector (a first bag dust removal structure 24 and a second bag dust removal structure 34), an induced draft fan (a first induced draft fan 28 and a second induced draft fan 35), a chimney (exhaust equipment) and multiple pipeline valves. The main equipment is evenly divided into two sets, one for use and one for backup (a first dust removal pipeline assembly 20 and a second dust removal pipeline assembly 30). This solution is: the flue gas is sent into the cyclone dust collector through the flue (inlet pipeline 10), most of the particulate matter in the flue gas is filtered and removed, and then the flue gas is cooled to about 110°C through the multi-tube heat exchanger and enters the bag dust collector for dust removal treatment. Finally, the qualified flue gas after treatment by the induced draft fan is discharged into the atmosphere through the chimney, and an additional set of bypass (spare pipeline 40) is added as an emergency backup in case of equipment failure. The 1500℃ kiln flue gas is sent to the dust removal equipment system through the underground flue to supplement the cold air. The temperature of the connected treatment is about 400℃. It is added with a quicklime spraying device through the cyclone dust collector to take away most of the boron-containing sticky substances. The dust removal mechanism makes the dust-laden air flow rotate, and the dust particles are separated from the air flow by centrifugal force and captured on the wall of the device. Then, the dust particles fall into the ash hopper with the help of gravity. The ash hopper is equipped with an ash discharge valve to discharge ash regularly. After being processed by the cyclone dust collector, it enters the multi-tube heat exchanger to cool the flue gas to about 110℃. The flue gas then enters the bag dust collector for The principle of crystallization treatment is that the filter bag is made of textile filter cloth or non-textile felt, and the dust-laden gas is filtered by the filtering effect of the fiber fabric. When the dust-laden gas enters the bag dust collector, the dust with large particles and high specific gravity settles down due to the action of gravity and falls into the ash hopper. When the gas containing finer dust passes through the filter material, the dust is retained, so that the gas is purified. The dust collector hopper is equipped with an ash discharge valve to discharge ash regularly. After being processed by a series of equipment and drawn out by the induced draft fan, the qualified flue gas is discharged into the atmosphere through the chimney. In addition, this method will set the equipment as two parallel systems, adopting a one-in-one standby operation mode to improve the operating stability of the equipment, increase the bypass pipeline to prepare for the simultaneous use of two sets of equipment in case of failure, and ensure the stable operation of the kiln. This technical solution uses a cyclone dust collector and spraying quicklime to remove a large amount of boron-containing sticky substances in the flue gas, which can greatly reduce the viscosity of the flue gas entering the bag dust collector, improve the standard of flue gas emission, reduce the probability of flue gas sticking to the equipment, and reduce the equipment operation and maintenance costs and maintenance frequency.

[0047] Thus far, various embodiments of the present application have been described in detail. To avoid obscuring the concept of the present application, some details well known in the art have not been described. Based on the above description, those skilled in the art can fully understand how to implement the technical solutions of this application.

[0048] Although some specific embodiments of the present application have been described in detail through examples, those skilled in the art will understand that the above examples are for illustrative purposes only and are not intended to limit the scope of the present application. Those skilled in the art will understand that the above embodiments may be modified or some technical features may be replaced by equivalents without departing from the scope and spirit of the present application. In particular, as long as there are no structural conflicts, the various technical features mentioned in the various embodiments may be combined in any manner.

Claims

1. A glass furnace fume treatment device, characterized in that: include: An air intake pipeline (10), wherein a first end of the air intake pipeline (10) is connected to an air outlet of a glass furnace flue, and a second end of the air intake pipeline (10) has a first branch (11), a second branch (12), and a third branch (13); a first dust removal pipeline assembly (20), the first dust removal pipeline assembly (20) being in communication with the first branch (11), the first dust removal pipeline assembly (20) being in communication with an exhaust device, and a first valve being disposed on the first dust removal pipeline assembly (20); a second dust removal pipeline assembly (30), the second dust removal pipeline assembly (30) being in communication with the second branch (12), the second dust removal pipeline assembly (30) being in communication with the exhaust device, and a second valve being disposed on the second dust removal pipeline assembly (30); A spare pipeline (40), the spare pipeline (40) is connected to the third branch (13), the spare pipeline (40) is connected to the exhaust device, and a third valve is arranged on the spare pipeline (40).

2. The glass furnace fume treatment device according to claim 1, characterized in that: The first dust removal pipeline assembly (20) comprises a first dust removal pipeline (21), a first cyclone dust removal structure (22), a first cooling structure (23) and a first bag dust removal structure (24); the first end of the first dust removal pipeline (21) is connected to the first branch (11); the first cyclone dust removal structure (22), the first cooling structure (23) and the first bag dust removal structure (24) are arranged in sequence from the first end of the first dust removal pipeline (21) to the second end of the first dust removal pipeline (21).

3. The glass furnace fume treatment device according to claim 2, characterized in that: The second dust removal pipeline assembly (30) comprises a second dust removal pipeline (31), a second cyclone dust removal structure (32), a second cooling structure (33) and a second bag dust removal structure (34); the first end of the second dust removal pipeline (31) is connected to the second branch (12); the second cyclone dust removal structure (32), the second cooling structure (33) and the second bag dust removal structure (34) are arranged in sequence from the first end of the second dust removal pipeline (31) to the second end of the second dust removal pipeline (31).

4. The glass furnace fume treatment device according to claim 2, characterized in that: The first cyclone dust removal structure (22) comprises a first air inlet (221), a first air outlet (222), a first dust removal bin (223) and a first feed pipeline (224); the first air inlet (221) is connected to the first dust removal bin (223); the first air outlet (222) is connected to the first dust removal bin (223); a first end of the first feed pipeline (224) is connected to the first dust removal bin (223); and a second end of the first feed pipeline (224) is connected to a quicklime discharge device.

5. The glass furnace fume treatment device according to claim 3, characterized in that: The second cyclone dust removal structure (32) comprises a second air inlet (321), a second air outlet (322), a second dust removal bin (323) and a second feed pipeline (324); the second air inlet (321) is connected to the second dust removal bin (323); the second air outlet (322) is connected to the second dust removal bin (323); the first end of the second feed pipeline (324) is connected to the second dust removal bin (323); and the second end of the second feed pipeline (324) is connected to the quicklime discharge device.

6. The glass furnace fume treatment device according to claim 3, characterized in that: The first end of the standby pipeline (40) is connected to the third branch (13), the second end of the standby pipeline (40) comprises a fourth branch (41) and a fifth branch (42), the fourth branch (41) is connected to the first dust removal pipeline (21), a fourth valve is arranged on the fourth branch (41), the fifth branch (42) is connected to the second dust removal pipeline (31), a fifth valve is arranged on the fifth branch (42).

7. The glass furnace fume treatment device according to claim 3, characterized in that: The first dust removal pipeline assembly (20) also includes a sixth branch (25), a first end of the sixth branch (25) is located between the first cyclone dust removal structure (22) and the first cooling structure (23) and is connected to the first dust removal pipeline (21), a second end of the sixth branch (25) is located between the second cyclone dust removal structure (32) and the second cooling structure (33) and is connected to the second dust removal pipeline (31), and a sixth valve is provided on the sixth branch (25).

8. The glass furnace fume treatment device according to claim 3, characterized in that: The first dust removal pipeline assembly (20) also includes a seventh branch (26), a first end of the seventh branch (26) is located between the first cooling structure (23) and the first bag dust removal structure (24) and is connected to the first dust removal pipeline (21), a second end of the seventh branch (26) is located between the second cooling structure (33) and the second bag dust removal structure (34) and is connected to the second dust removal pipeline (31), and a seventh valve is provided on the seventh branch (26).

9. The glass furnace fume treatment device according to claim 3, characterized in that: The first dust removal pipeline assembly (20) further includes an eighth branch (27), a first end of the eighth branch (27) being located between the first bag dust removal structure (24) and the exhaust device and being connected to the first dust removal pipeline (21), a second end of the eighth branch (27) being located between the second bag dust removal structure (34) and the exhaust device and being connected to the second dust removal pipeline (31), and an eighth valve being provided on the eighth branch (27).

10. The glass furnace fume treatment device according to claim 2, characterized in that: The first dust removal pipeline assembly (20) further comprises a first induced draft fan (28), wherein the first induced draft fan (28) is arranged on the first dust removal pipeline (21), and the first induced draft fan (28) is located on a side of the first bag dust removal structure (24) close to the second end of the first dust removal pipeline (21).

Images