Efficient SDS (sodium dodecyl sulfate) desulfurizing tower
By introducing a whirlwind desulfurization tower and a low -voltage pulse blowing bag dust collector in the desulfurization tower, the problem of insufficient flue gas response in the shell tower is solved, and a more efficient sulfur removal effect is achieved.
Patent Information
- Application Number
- CN202421112952.8
- Authority / Receiving Office
- CN · China
- Patent Type
- Utility models(China)
- Current Assignee / Owner
- Filing Date
- 2024-05-21
- Publication Date
- 2025-01-24
- Estimated Expiration
- 2034-05-21
AI Technical Summary
The existing desulfurization towers are hollow shell towers, which cause the flue gas mixture to react inadequately and cannot effectively remove sulfur dioxide from the flue gas.
A high -efficiency SDS desulfurization tower is designed, which uses a whirlwind desulfurization tower and a low -voltage pulse spray bag -type dust collector to fully mix and deal with the smoke through the whirlwind separator and the conveyor tube.
It achieves a more complete reaction of the flue gas mixture in the desulfurization tower, improves the desulfurization efficiency, ensures that sulfur dioxide in the flue gas is effectively removed, and achieves efficient desulfurization.
Smart Images
Figure CN222384471U_ABST
Abstract
Description
Technical Field
[0001] The utility model belongs to the technical field of desulfurization towers and relates to a high-efficiency SDS desulfurization tower. Background Art
[0002] The SDS desulfurization process mainly involves spraying powdered fixed active calcium or sodium bicarbonate into the boiler flue gas and fully mixing it with the flue gas, converting the gaseous SO2 into granular calcium sulfate under high temperature and high humidity conditions, thereby achieving the removal of SO2 from the flue gas. The core of this process is to convert SO2 into recyclable calcium sulfate products by a dry method during the flue gas treatment process, and further reduce the impact of fossil fuel combustion emissions on the environment.
[0003] When the existing desulfurization tower is used, its function is to reduce the sulfur dioxide emission in the industrial waste gas. The desulfurization effect is achieved by preparing different desulfurizers. However, the previous desulfurization towers are empty shell towers, and the flue gas mixture does not react sufficiently in them. Utility Model Content
[0004] In view of this, the purpose of the present invention is to provide a high-efficiency SDS desulfurization tower to solve the problem mentioned in the above background technology that the previous desulfurization towers are all empty shell towers and the flue gas mixture does not react sufficiently therein.
[0005] In order to achieve the above-mentioned purpose, the utility model provides the following technical solutions: a high-efficiency SDS desulfurization tower, comprising a flue, a cyclone desulfurization tower, a low-pressure pulse jet bag dust collector and a chimney connected in sequence; the flue gas is tangentially connected to the interior of the cyclone desulfurization tower through the flue, and a grinder is connected to the flue through a docking pipe, and a conveying fan is also provided on the docking pipe. The grinder grinds baking soda into fine powder, which is delivered to the docking pipe from the conveying fan.
[0006] Optionally, a cyclone separator is provided in the cyclone desulfurization tower.
[0007] Optionally, a conveying pipe is provided between the cyclone desulfurization tower and the low-pressure pulse jet bag filter for connection.
[0008] Optionally, an induced draft fan for extracting flue gas is provided between the low-pressure pulse jet bag filter and the chimney.
[0009] The beneficial effects of the utility model are as follows: the high-efficiency SDS desulfurization tower of the utility model enters the flue connected to one side of the cyclone desulfurization tower through the flue gas from the docking pipe, and the baking soda powder is ground into fine powder by a grinder and delivered to the flue by a self-conveying fan, and the flue gas after the baking soda and the flue gas are mixed enters the cyclone desulfurization tower along the tangential direction. In the past, desulfurization towers were all empty shell towers. The cyclone desulfurization tower applies the principle of cyclone separators to make the flue gas mixture react more fully therein. After desulfurization, the flue gas enters the low-pressure pulse jet bag dust collector along the conveying pipe for dust removal, and then the flue gas in the low-pressure pulse jet bag dust collector is extracted by the induced draft fan, so that it is discharged from the chimney into the atmosphere, thereby achieving a more efficient desulfurization effect with a more complete reaction of the flue gas mixture.
[0010] Other advantages, objectives and features of the present invention will be described in the following description to some extent, and will be apparent to those skilled in the art based on the following examination and research, or can be taught from the practice of the present invention to some extent. The objectives and other advantages of the present invention can be achieved and obtained through the following description. BRIEF DESCRIPTION OF THE DRAWINGS
[0011] In order to make the purpose, technical solution and advantages of the utility model clearer, the utility model will be described in detail below in conjunction with the accompanying drawings, in which:
[0012] Figure 1 It is a schematic diagram of the overall structure of the present invention;
[0013] Figure 2 It is the front view of the present invention.
[0014] Figure numerals: 1. docking pipe; 2. flue; 3. cyclone desulfurization tower; 4. conveying fan; 5. grinder; 6. conveying pipe; 7. low-pressure pulse jet bag dust collector; 8. chimney; 9. induced draft fan. DETAILED DESCRIPTION
[0015] The following describes the implementation of the present invention through specific examples. Those skilled in the art can easily understand other advantages and effects of the present invention from the contents disclosed in this specification. The present invention can also be implemented or applied through other different specific implementations, and the details in this specification can also be modified or changed in various ways based on different viewpoints and applications without departing from the spirit of the present invention. It should be noted that the illustrations provided in the following embodiments only illustrate the basic concept of the present invention in a schematic manner. The following embodiments and the features in the embodiments can be combined with each other without conflict.
[0016] Among them, the drawings are only used for illustrative explanations, and they only represent schematic diagrams rather than actual pictures, and should not be understood as limitations on the present utility model. In order to better illustrate the embodiments of the present utility model, some parts of the drawings may be omitted, enlarged or reduced, and do not represent the size of the actual product. For those skilled in the art, it is understandable that some well-known structures and their descriptions in the drawings may be omitted.
[0017] The same or similar numbers in the drawings of the embodiments of the present invention correspond to the same or similar parts; in the description of the present invention, it should be understood that if the terms "upper", "lower", "left", "right", "front", "back" and the like indicate directions or positional relationships, they are based on the directions or positional relationships shown in the drawings, which are only for the convenience of describing the present invention and simplifying the description, rather than indicating or implying that the device or element referred to must have a specific direction, be constructed and operated in a specific direction. Therefore, the terms describing the positional relationship in the drawings are only used for illustrative purposes and cannot be understood as a limitation on the present invention. For ordinary technicians in this field, the specific meanings of the above terms can be understood according to specific circumstances.
[0018] See also Figure 1-2 , which is a high-efficiency SDS desulfurization tower, includes a docking pipe 1: one end of the docking pipe 1 is connected to a flue 2, one end of the flue 2 is connected to a cyclone desulfurization tower 3, a conveying fan 4 is arranged on one side of the docking pipe 1, a grinder 5 is connected to one side of the conveying fan 4, a conveying pipe 6 is connected to the top of the cyclone desulfurization tower 3, one end of the conveying pipe 6 is connected to a low-pressure pulse jet bag dust collector 7, a draft fan 9 is arranged on one side of the low-pressure pulse jet bag dust collector 7, a chimney 8 is arranged on one side of the induced draft fan 9, and the dust removal components in the low-pressure pulse jet bag dust collector 7 are prior art and can be purchased on the market. They are not used as technical protection points of this application, so no excessive statements are made.
[0019] In this embodiment, the grinder 5 grinds the baking soda into fine powder, and the baking soda ground into fine powder by the grinder 5 is delivered to the docking pipe 1 from the conveying fan 4, so that the baking soda ground into fine powder by the grinder 5 is delivered to the inside of the docking pipe 1 through the conveying fan 4.
[0020] In this embodiment, the cyclone desulfurization tower 3 itself applies the principle of the cyclone separator, and the cyclone desulfurization tower 3 applies the principle of the cyclone separator, so that the flue gas mixture reacts more fully therein. The cyclone desulfurization tower 3 and the low-pressure pulse jet bag dust collector 7 are connected by a conveying pipe 6, so that the cyclone desulfurization tower 3 and the low-pressure pulse jet bag dust collector 7 are connected by the conveying pipe 6. The flue gas in the cyclone desulfurization tower 3 is transported to the inside of the low-pressure pulse jet bag dust collector 7 through the conveying pipe 6, so that the flue gas in the cyclone desulfurization tower 3 is transported to the low-pressure pulse jet bag dust collector 7 through the conveying pipe 6 for subsequent treatment. The low-pressure pulse jet bag dust collector 7 performs dust removal on the flue gas after desulfurization, and the low-pressure pulse jet bag dust collector 7 performs dust removal on the flue gas. The induced draft fan 9 extracts the flue gas in the chimney 8, so that the induced draft fan 9 is used to assist in extracting the flue gas in the chimney 8.
[0021] Working principle: When the desulfurization tower is subjected to efficient desulfurization, the flue gas enters the flue 2 connected to one side of the cyclone desulfurization tower 3 through the docking pipe 1, and the baking soda powder is ground into fine powder by the grinder 5 and delivered to the flue 2 from the conveying fan 4. The flue gas after the baking soda and the flue gas are mixed enters the cyclone desulfurization tower 3 along the tangential direction. In the past, desulfurization towers were all empty shell towers. The cyclone desulfurization tower 3 applies the principle of cyclone separator to make the flue gas mixture react more fully. After desulfurization, the flue gas enters the low-pressure pulse jet bag filter 7 along the conveying pipe 6 for dust removal, and then the flue gas in the low-pressure pulse jet bag filter 7 is extracted by the induced draft fan 9 and discharged into the atmosphere from the chimney 8, thereby achieving a more efficient desulfurization effect with a more complete reaction of the flue gas mixture.
[0022] Finally, 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 purpose and scope of the technical solution, which should be included in the scope of the claims of the utility model.
Claims
1. High-efficiency SDS desulfurization tower, characterized by: It includes a flue, a cyclone desulfurization tower, a low-pressure pulse jet bag dust collector and a chimney connected in sequence; the flue gas is tangentially connected to the inside of the cyclone desulfurization tower through the flue, and the flue is connected to a grinder through a docking pipe, and a conveying fan is also provided on the docking pipe. The grinder grinds baking soda into fine powder and delivers it to the docking pipe from the conveying fan.
2. The high-efficiency SDS desulfurization tower according to claim 1 is characterized in that: A cyclone separator is provided in the cyclone desulfurization tower.
3. The high-efficiency SDS desulfurization tower according to claim 1 is characterized in that: A conveying pipe is provided between the cyclone desulfurization tower and the low-pressure pulse jet bag dust collector for connection.
4. The high-efficiency SDS desulfurization tower according to claim 1 is characterized in that: An induced draft fan for extracting flue gas is also provided between the low-pressure pulse jet bag filter and the chimney.