Flue gas desulfurization absorption tower
By designing the flue duct and optimizing the airflow distribution of the flue gas desulfurization absorption tower, the problem of increasing costs in the existing technology is solved, and a more efficient and economical desulfurization effect is achieved, and the production costs of enterprises are reduced.
Patent Information
- Application Number
- CN202421410131.2
- Authority / Receiving Office
- CN · China
- Patent Type
- Utility models(China)
- Current Assignee / Owner
- Filing Date
- 2024-06-20
- Publication Date
- 2025-03-25
- Estimated Expiration
- 2034-06-20
AI Technical Summary
When the existing flue gas desulfurization absorption towers face increasingly stringent environmental protection requirements, their costs have increased, becoming a major player in power plant operation costs, increasing the production pressure of enterprises.
By rationally designing the flue size and shape of the absorption tower, the pressure loss of the desulfurization tower equipment is reduced, the airflow distribution design is optimized, and key process parameters such as the optimal empty tower speed and gas residence time are determined to achieve maximum desulfurization efficiency.
It has achieved a more economical and energy-saving desulfurization effect, providing reliable guarantees for the economic and high-quality operation of the desulfurization system, and at the same time reducing the production costs of enterprises.
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Figure CN222658266U_ABST
Abstract
Description
Technical Field
[0001] The utility model relates to the technical field of desulfurization absorption towers, in particular to a flue gas desulfurization absorption tower. Background Art
[0002] In order to protect the environment and reduce air pollution, most thermal power companies need to desulfurize the flue gas before discharging it into the atmosphere. The desulfurization tower is a tower equipment for desulfurizing industrial waste gas. The desulfurization tower was originally built with granite and was the most widely used. It uses the principle of water film desulfurization and dust removal. The advantage is that it is easy to maintain, and it can achieve the effect of dust removal and desulfurization at the same time by preparing different dust removal agents. With the development of FRP technology, desulfurization towers are gradually changed to be made of FRP. Compared with granite desulfurization towers, FRP desulfurization towers have low cost, easy processing, no rust and no rot, and light weight. Therefore, it has become the development trend of desulfurization towers in the future. In addition, stainless steel has the three advantages of corrosion resistance, high temperature resistance, and wear resistance, which is also one of the important development trends of desulfurization towers.
[0003] However, the existing flue gas desulfurization absorption towers have the problem of facing increasingly stringent environmental protection requirements, and the cost has increased accordingly. They have become a major contributor to the operating costs of power plants, increasing the production pressure of companies in the industry. Utility Model Content
[0004] The purpose of this section is to summarize some aspects of the embodiments of the utility model and briefly introduce some preferred embodiments. Some simplifications or omissions may be made in this section and the specification abstract and utility model name of this application to avoid blurring the purpose of this section, specification abstract and utility model name, and such simplifications or omissions cannot be used to limit the scope of the utility model.
[0005] In view of the fact that the above or existing technologies are faced with increasingly stringent environmental protection requirements, the cost increases accordingly, and have become a major contributor to the operating costs of power plants, increasing the production pressure of companies in the industry, the present utility model is proposed.
[0006] Therefore, the purpose of the utility model is to provide a flue gas desulfurization absorption tower.
[0007] In order to solve the above technical problems, the utility model provides the following technical solutions: a flue gas desulfurization absorption tower, comprising a main body, including a tower body, a tower head arranged at the upper end of the tower body, and a smoke inlet hole arranged at the lower side of the outer end of the tower body, an arc-shaped smoke inlet pipe is arranged in the smoke inlet hole, a water inlet hole and a rotating shaft hole are opened in the outer end of the tower body, a water delivery component is arranged in the water inlet hole, a driving component is arranged in the rotating shaft hole, and a desulfurization component is arranged inside the tower body.
[0008] As a preferred solution of the flue gas desulfurization absorption tower of the utility model, wherein: a T-shaped channel is opened inside the tower head, and the lower end surface of the T-shaped channel is connected to the internal channel of the tower body.
[0009] As a preferred solution of the flue gas desulfurization absorption tower of the utility model, the water delivery component includes a water inlet pipe arranged in the water inlet hole, a water storage tank arranged at the lower end of the water inlet pipe, and a fixed pipe arranged at the other end of the water inlet pipe, and a T-shaped groove is opened at the lower end of the fixed pipe.
[0010] As a preferred solution of the flue gas desulfurization absorption tower of the utility model, the driving assembly includes a rotating shaft arranged in the rotating shaft hole, a bevel gear arranged on one side of the rotating shaft close to the desulfurization assembly, and a motor arranged at the other end of the rotating shaft.
[0011] As a preferred solution of the flue gas desulfurization absorption tower of the utility model, the desulfurization component includes a smoke blocking plate arranged on the inner wall of the tower body, a drive shaft arranged at the bottom end of the tower body, and a bevel gear arranged on the outer wall of the drive shaft.
[0012] As a preferred solution of the flue gas desulfurization absorption tower of the utility model, wherein: a lower water pipe is arranged at the upper end of the bevel gear, a through plate is arranged on the outer wall of the lower water pipe, a first nozzle is arranged on the outer wall of the through plate, and a hollow plate is arranged inside the through plate.
[0013] As a preferred solution of the flue gas desulfurization absorption tower of the utility model, wherein: a threaded pipe is arranged at the upper end of the lower water pipe, an upper water pipe is arranged at the upper end of the threaded pipe, a disc is arranged at the upper end of the upper water pipe, the interior of the disc is arranged as a cavity structure, and a second nozzle is arranged at the lower end of the disc.
[0014] As a preferred solution of the flue gas desulfurization absorption tower of the utility model, wherein: a movable tube is arranged at the upper end of the disc, and a T-shaped clamp is arranged at the upper end of the movable tube.
[0015] The beneficial effects of the flue gas desulfurization absorption tower of the utility model: the utility model reasonably designs the size and shape of the absorption tower flue, reduces the pressure loss of the desulfurization tower equipment to a minimum, thereby minimizing the induced draft function consumption, accurately simulates the gas flow field in the absorption tower, adopts an optimized airflow distribution design, reasonably designs various elements such as the tower diameter and tower height, determines the optimal empty tower velocity, gas residence time and other key process parameters, and achieves maximum desulfurization efficiency, so that it can provide reliable guarantees for the economic and high-quality operation of the desulfurization system in a more economical and energy-saving way, while taking into account environmental protection and social benefits, further reducing the production costs of enterprises. BRIEF DESCRIPTION OF THE DRAWINGS
[0016] In order to more clearly illustrate the technical solutions of the embodiments of the present utility model, the following briefly introduces the drawings required for the description of the embodiments. Obviously, the drawings described below are only some embodiments of the present utility model. For ordinary technicians in this field, other drawings can be obtained based on these drawings without creative labor. Among them:
[0017] Figure 1 This is an overall schematic diagram of the main components of the flue gas desulfurization absorption tower.
[0018] Figure 2 This is a schematic diagram from another angle of the overall water supply component, drive component and desulfurization component for the flue gas desulfurization absorption tower.
[0019] Figure 3 This is an overall schematic diagram of the hollow plate used in the flue gas desulfurization absorption tower.
[0020] Figure 4 This is an overall schematic diagram of the T-slot and T-clip used for the flue gas desulfurization absorption tower.
[0021] 1. Main body; 11. Tower body; 12. Tower head; 13. Smoke inlet hole; 14. Curved smoke inlet pipe; 15. Water inlet hole; 16. Rotating shaft hole; 17. T-shaped channel;
[0022] 2. Water delivery assembly; 21. Water inlet pipe; 22. Water storage tank; 23. Fixed pipe; 24. T-slot;
[0023] 3. driving assembly; 31. rotating shaft; 32. bevel gear; 33. motor;
[0024] 4. Desulfurization assembly; 41. Smoke barrier; 42. Drive shaft; 43. Bevel gear; 44. Lower water pipe; 45. Through plate; 451. Hollow plate; 46. First nozzle; 47. Threaded pipe; 48. Upper water pipe; 49. Disc; 491. Second nozzle; 492. Movable pipe; 493. T-type clamp. DETAILED DESCRIPTION
[0025] In order to make the above-mentioned purposes, features and advantages of the present invention more obvious and easy to understand, the specific implementation methods of the present invention are described in detail below in conjunction with the accompanying drawings.
[0026] In the following description, many specific details are set forth to facilitate a full understanding of the present invention, but the present invention may also be implemented in other ways different from those described herein, and those skilled in the art may make similar generalizations without violating the connotation of the present invention. Therefore, the present invention is not limited to the specific embodiments disclosed below.
[0027] Secondly, the term "one embodiment" or "embodiment" as used herein refers to a specific feature, structure or characteristic that may be included in at least one implementation of the present invention. The term "in one embodiment" that appears in different places in this specification does not necessarily refer to the same embodiment, nor does it refer to a separate or selective embodiment that is mutually exclusive with other embodiments. Example 1
[0028] Reference Figure 1 , which is the first embodiment of the utility model, and this embodiment provides a flue gas desulfurization absorption tower, which can achieve a desulfurization effect, and includes a main body component 1, including a tower body 11, a tower head 12 arranged at the upper end of the tower body 11, and a smoke inlet 13 arranged at the lower side of the outer end of the tower body 11, an arc-shaped smoke inlet pipe 14 is arranged in the smoke inlet 13, a water inlet hole 15 and a rotating shaft hole 16 are opened at the outer end of the tower body 11, a water delivery component 2 is arranged in the water inlet hole 15, a driving component 3 is arranged in the rotating shaft hole 16, and a desulfurization component 4 is arranged inside the tower body 11.
[0029] Specifically, a T-shaped channel 17 is opened inside the tower head 12 , and the lower end surface of the T-shaped channel 17 is connected to the internal channel of the tower body 11 .
[0030] Furthermore, the curved smoke inlet pipe 14 is designed, and the flat structure is conducive to the flow of smoke, reduces resistance, and improves the efficiency of the flue. The main reasons are as follows: Optimization of flow characteristics: The flat flue structure reduces the bends and mutations of the flow, making it easier for the smoke to flow along the design direction, which avoids unnecessary vortices and turbulence, because they will increase the resistance of the flow; Reduce mutations: In traditional circular or cylindrical flues, the flow of smoke often produces vortices at turns or cross-sectional changes. These vortices not only increase the resistance of the flow, but may also cause the separation of the smoke and affect the stability of the smoke flow. The flat flue structure reduces such flow mutations, thereby reducing resistance; Cross-sectional optimization: The cross-sectional area of the flat flue is relatively small, which means that the friction between the gas and the flue wall during the flow process is reduced. This design can significantly reduce the flow resistance, thereby improving the flow efficiency of the smoke; Design flexibility: The flat flue structure allows the designer to optimize the length and width of the flue according to actual needs, so as to better adapt to various application scenarios and working conditions. This flexibility helps to further improve the efficiency of the flue. Structural stability: The flat structural design also improves the structural stability of the flue. Due to its shape and material selection, the flat flue can withstand greater gas pressure and temperature changes, reducing the additional resistance caused by structural instability. In summary, the flat structure effectively reduces flow resistance and improves the efficiency of the flue by optimizing the flow characteristics of flue gas, reducing mutations, cross-sectional optimization, design flexibility and structural stability. This design has been widely used in industrial desulfurization tower equipment because it helps reduce energy consumption and maintenance costs and improve the overall efficiency of the equipment.
[0031] Furthermore, the T-shaped channel 17 opened inside the tower head 12 can reduce the resistance of the airflow and lower the pressure drop, thereby increasing the speed and efficiency of the flue gas passing through the desulfurization tower.
[0032] Furthermore, the driving component 3 drives the desulfurization component 4 to operate, so that the desulfurization tower has a desulfurization function. With the help of the setting of the water delivery component 2, the desulfurization effect is enhanced and the practicality is improved.
[0033] In summary, by reasonably designing the size and shape of the absorption tower flue, the pressure loss of the desulfurization tower equipment is reduced to a minimum, thereby minimizing the induced draft function consumption. By accurately simulating the gas flow field in the absorption tower and adopting an optimized airflow distribution design, the tower diameter, tower height and other factors are reasonably designed, and the optimal empty tower velocity, gas residence time and other key process parameters are determined to achieve maximum desulfurization efficiency. This provides reliable guarantees for the economic and high-quality operation of the desulfurization system in a more economical and energy-saving way, while taking into account environmental protection and social benefits, and further reducing the production costs of the enterprise. Example 2
[0034] Reference Figure 2 , which is the second embodiment of the utility model. Different from the previous embodiment, this embodiment provides a multifunctional operation guarantee for the flue gas desulfurization absorption tower, which includes a water delivery component 2 including a water inlet pipe 21 arranged in the water inlet hole 15, a water storage tank 22 arranged at the lower end of the water inlet pipe 21, and a fixed pipe 23 arranged at the other end of the water inlet pipe 21, and a T-shaped groove 24 is opened at the lower end of the fixed pipe 23.
[0035] Specifically, the driving assembly 3 includes a rotating shaft 31 disposed in the rotating shaft hole 16 , a bevel gear 32 disposed on one side of the rotating shaft 31 close to the desulfurization assembly 4 , and a motor 33 disposed on the other end of the rotating shaft 31 .
[0036] Specifically, the desulfurization assembly 4 includes a smoke blocking plate 41 arranged on the inner wall of the tower body 11 , a threaded shaft 42 arranged at the bottom end of the inner part of the tower body 11 , and a bevel gear 43 arranged on the outer wall of the threaded shaft 42 .
[0037] Specifically, a threaded pipe 47 is provided at the upper end of the lower water pipe 44, an upper water pipe 48 is provided at the upper end of the threaded pipe 47, a disc 49 is provided at the upper end of the upper water pipe 48, the interior of the disc 49 is provided as a cavity structure, and a second nozzle 491 is provided at the lower end of the disc 49.
[0038] Furthermore, the lower water pipe 44 is threadedly connected to the threaded shaft 42 to achieve up and down lifting movement, thereby providing a power source for the up and down movement of the lower water pipe 44 .
[0039] Furthermore, the water inlet pipe 21 is designed as an L-shaped structure, the fixed pipe 23 is connected to one end of the water inlet pipe 21, and the other end of the water inlet pipe 21 is connected to the water storage tank 22, thereby providing operation guarantee for the water transportation in the upper water pipe 48 on the lower side of the fixed pipe 23.
[0040] Furthermore, the motor 33 drives the rotating shaft 31 to rotate, driving the bevel gear 32 to rotate. Since the bevel gear 32 is meshed with the helical gear 43, the threaded shaft 42 is driven to rotate, providing driving force for the up and down movement of the lower water pipe 44.
[0041] Furthermore, the provision of the smoke barrier 41 is conducive to preventing the spread of fire: when a fire occurs, the smoke barrier can effectively slow down the spread of the fire, buying precious time for personnel evacuation and fire rescue; reducing smoke emissions: the smoke barrier can reduce the generation of smoke during the combustion process, thereby reducing the damage caused by inhaling toxic smoke; environmental protection and health: in the process of producing flame retardant boards, due to the integrity of the wood, the use of liquid glue can be reduced, thereby reducing the content of harmful substances such as formaldehyde, making it more environmentally friendly and healthy; diversified performance: in addition to being flame retardant, the smoke barrier also has the characteristics of smoke suppression, corrosion resistance, insect resistance and stability. These properties make the smoke barrier more and more popular in modern decoration; light weight and easy processing: the smoke barrier is made of plywood, which is light and easy to process, convenient to construct, and can effectively reduce costs.
[0042] Furthermore, the provision of the threaded tube 47 is beneficial for improving the sealing and ductility of the connection between the lower water pipe 44 and the upper water pipe 48 by means of the tensile elasticity of the threaded tube 47 when the lower water pipe 44 moves downward.
[0043] In summary, the tower diameter, tower height and other factors are reasonably designed, and the key process parameters such as the optimal empty tower velocity and gas residence time are determined to achieve the maximum desulfurization efficiency. According to the actual working conditions, the number of spray layers and layer height are optimized to determine the optimal spray density and improve the spray coverage. The gas flow field in the absorption tower is accurately simulated, and an optimized airflow distribution design is adopted to ensure uniform distribution of the fluid in the tower. Example 3
[0044] Reference Figure 3-4 , which is the third embodiment of the utility model. Different from the previous embodiment, this embodiment provides a linkage effect guarantee for the flue gas desulfurization absorption tower, which includes a lower water pipe 44 provided at the upper end of the bevel gear 43, a through plate 45 provided on the outer wall of the lower water pipe 44, a first nozzle 46 provided on the outer wall of the through plate 45, and a hollow plate 451 provided inside the through plate 45.
[0045] Specifically, a movable tube 492 is provided at the upper end of the disc 49 , and a T-shaped clamp 493 is provided at the upper end of the movable tube 492 .
[0046] Furthermore, the rotation of the desulfurization component 4 is achieved by means of the mutual engagement of the T-slot 24 and the T-clip 493 .
[0047] Furthermore, a plurality of through plates 45 are arranged in a circular array along the center of the lower water delivery pipe 44 , and a plurality of first nozzles 46 are arranged in a linear array on a horizontal line of the through plates 45 .
[0048] Furthermore, the setting of the hollow plate 451, on the one hand, prevents the water of the upper water pipe 48 from directly flowing into the lower water pipe 44 below, thereby achieving the spraying effect on the first nozzle 46 on the through plate 45, and on the other hand, through the hollow setting, guides the water into the lower water pipe 44 below, thereby increasing the water source for the spraying of the second nozzle 491.
[0049] Furthermore, when the threaded shaft 42 rotates, it drives the lower water pipe 44 to rotate while realizing up and down lifting movements. When the lower water pipe 44 rotates, with the help of the fixed connection between the lower water pipe 44 and the upper water pipe 48, the disc 49 and the movable pipe 492, the lower water pipe 44 and the upper water pipe 48, the disc 49 and the movable pipe 492 and other components are driven to rotate, thereby improving the range and effect of the spraying.
[0050] In summary, the staff turns on the driving component 3 to drive the desulfurization component 4 to move, thereby achieving the desulfurization effect on the absorption tower. With the help of the setting of the water delivery component 2, the spraying effect is enhanced and the desulfurization efficiency is maximized, so that it can provide reliable guarantees for the economic and high-quality operation of the desulfurization system in a more economical and energy-saving way, while taking into account environmental protection and social benefits, further reducing the production costs of the enterprise.
[0051] Importantly, it should be noted that the construction and arrangement of the present application shown in a number of different exemplary embodiments are only exemplary. Although only a few embodiments are described in detail in this disclosure, it should be readily understood by those who refer to this disclosure that many modifications are possible (e.g., the size, scale, structure, shape and proportion of various elements, and parameter values (e.g., temperature, pressure, etc.), mounting arrangements, use of materials, color, directional changes, etc.) without substantially departing from the novel teachings and advantages of the subject matter described in the application. For example, an element shown as integrally formed may be composed of multiple parts or elements, the position of the element may be inverted or otherwise changed, and the nature or number or position of the discrete element may be changed or changed. Therefore, all such modifications are intended to be included in the scope of the present utility model. The order or sequence of any process or method steps may be changed or reordered according to alternative embodiments. In the claims, any "device plus function" clause is intended to cover the structure described herein that performs the function, and is not only structurally equivalent but also an equivalent structure. Without departing from the scope of the present invention, other substitutions, modifications, changes and omissions may be made in the design, operating conditions and arrangement of the exemplary embodiments. Therefore, the present invention is not limited to a specific embodiment, but extends to various modifications that still fall within the scope of the appended claims.
[0052] Additionally, in order to provide a concise description of example embodiments, all features of an actual embodiment may not be described (ie, those features that are not relevant to the best mode presently contemplated for carrying out the invention or those that are not relevant to implementing the invention).
[0053] It will be appreciated that in the development of any actual implementation, as in any engineering or design project, numerous implementation-specific decisions may be made. Such a development effort may be complex and time-consuming, but will be a routine task of design, fabrication, and production for those of ordinary skill having the benefit of this disclosure without undue experimentation.
[0054] It should be noted that the above embodiments are only used to illustrate the technical solution of the utility model rather than to limit it. Although the utility model has been described in detail with reference to the preferred embodiments, ordinary technicians in the field should understand that the technical solution of the utility model can be modified or replaced by equivalents without departing from the spirit and scope of the technical solution of the utility model, which should be included in the scope of the claims of the utility model.
Claims
1. A flue gas desulfurization absorption tower, characterized in that: include, The main body component (1) comprises a tower body (11), a tower head (12) arranged at the upper end of the tower body (11), and a smoke inlet hole (13) arranged at the lower side of the outer end of the tower body (11); an arc-shaped smoke inlet pipe (14) is arranged in the smoke inlet hole (13); a water inlet hole (15) and a rotating shaft hole (16) are opened at the outer end of the tower body (11); a water delivery component (2) is arranged in the water inlet hole (15); a driving component (3) is arranged in the rotating shaft hole (16); and a desulfurization component (4) is arranged inside the tower body (11).
2. The flue gas desulfurization absorption tower according to claim 1, characterized in that: A T-shaped channel (17) is provided inside the tower head (12), and the lower end surface of the T-shaped channel (17) is connected to the internal channel of the tower body (11).
3. The flue gas desulfurization absorption tower according to claim 1, characterized in that: The water delivery assembly (2) comprises a water inlet pipe (21) arranged in the water inlet hole (15), a water storage tank (22) arranged at the lower end of the water inlet pipe (21), and a fixed pipe (23) arranged at the other end of the water inlet pipe (21), wherein a T-shaped groove (24) is provided at the lower end of the fixed pipe (23).
4. The flue gas desulfurization absorption tower according to claim 1, characterized in that: The driving assembly (3) comprises a rotating shaft (31) arranged in the rotating shaft hole (16), a bevel gear (32) arranged on a side of the rotating shaft (31) close to the desulfurization assembly (4), and a motor (33) arranged at the other end of the rotating shaft (31).
5. The flue gas desulfurization absorption tower according to claim 4, characterized in that: The desulfurization assembly (4) comprises a smoke blocking plate (41) arranged on the inner wall of the tower body (11), a driving shaft (42) arranged at the bottom end inside the tower body (11), and a bevel gear (43) arranged on the outer wall of the driving shaft (42).
6. The flue gas desulfurization absorption tower according to claim 5, characterized in that: A lower water delivery pipe (44) is provided at the upper end of the bevel gear (43), a through plate (45) is provided on the outer wall of the lower water delivery pipe (44), a first nozzle (46) is provided on the outer wall of the through plate (45), and a hollow plate (451) is provided inside the through plate (45).
7. The flue gas desulfurization absorption tower according to claim 6, characterized in that: The upper end of the lower water delivery pipe (44) is provided with a threaded pipe (47), the upper end of the threaded pipe (47) is provided with an upper water delivery pipe (48), the upper end of the upper water delivery pipe (48) is provided with a disc (49), the interior of the disc (49) is provided with a cavity structure, and the lower end of the disc (49) is provided with a second nozzle (491).
8. The flue gas desulfurization absorption tower according to claim 7, characterized in that: A movable tube (492) is provided at the upper end of the disc (49), and a T-shaped clamp (493) is provided at the upper end of the movable tube (492).