Dust removal equipment of flue gas desulfurization tower
By installing spiral slices in the processing cavity of the flue gas desulfurization tower, the flue gas is forced to flow in a spiral manner, solve the problem of insufficient response to the flue gas and desulfurization solution, improves the desulfurization effect, and uses the secondary utilization to reduce the desulfurization solution. waste.
Patent Information
- Application Number
- CN202420748586.9
- Authority / Receiving Office
- CN · China
- Patent Type
- Utility models(China)
- Current Assignee / Owner
- Filing Date
- 2024-04-11
- Publication Date
- 2025-01-24
- Estimated Expiration
- 2034-04-11
AI Technical Summary
The flue gas flows rapidly in traditional flue gas desulfurization towers, resulting in insufficient reaction between the flue gas and the desulfurization liquid and poor desulfurization effect.
Install spiral slices in the processing cavity of the flue gas desulfurization tower, forcing flue gas to flow in a spiral manner, increasing the contact time and opportunity of flue gas and desulfurization solution. At the same time, a flowing liquid hole is set on the partition to allow desulfurization fluid to use secondary utilization to reduce waste.
By increasing the residence time of flue gas in the tower body, the reaction effect between flue gas and desulfurization liquid is improved, the efficiency of flue gas desulfurization is improved, and the waste of desulfurization liquid is reduced through secondary utilization.
Smart Images

Figure CN222384528U_ABST
Abstract
Description
Technical Field
[0001] The utility model relates to the technical field of flue gas treatment, in particular to dust removal equipment for a flue gas desulfurization tower. Background Art
[0002] The desulfurization tower is a tower-type equipment for desulfurization of industrial waste gas. The desulfurization tower was originally built with granite and was most widely used. It uses the principle of water film desulfurization and dust removal, and is also known as granite water film desulfurization dust collector, or granite water film desulfurization dust collector.
[0003] The flue gas in a traditional desulfurization tower usually flows directly upward, causing the flue gas to stay in the desulfurization tower for too short a time, resulting in insufficient reaction between the desulfurization liquid sprayed from the nozzle and the flue gas, resulting in poor flue gas desulfurization effect.
[0004] Therefore, we proposed a dust removal equipment for a flue gas desulfurization tower in order to solve the above-mentioned problems. Utility Model Content
[0005] The utility model aims to solve the problem that the reaction effect between smoke and smoke removal solution is relatively poor.
[0006] To achieve the above-mentioned purpose, the utility model adopts the following technical scheme: a dust removal device for a flue gas desulfurization tower, comprising a tower body, wherein a processing chamber and a liquid storage chamber are sequentially arranged inside the tower body from top to bottom, a cylinder is installed inside the processing chamber, a spiral sheet is installed on the outer surface of the cylinder, a water pump is installed inside the cylinder, a liquid suction pipe extending into the liquid storage chamber is installed at the water pumping end of the water pump, a spiral liquid spray pipe is installed at the water outlet end of the water pump, and a plurality of nozzles extending to the outside of the cylinder are installed on the outer surface of the liquid spray pipe.
[0007] Furthermore: a partition is arranged between the processing chamber and the liquid storage chamber, and a plurality of liquid flow holes are opened on the partition, and a plurality of liquid flow holes are located outside the cylinder.
[0008] Furthermore: a smoke inlet pipe communicating with the processing chamber is installed on the outer surface of the tower body, and one end of the smoke inlet pipe is fixedly connected to the outer surface of the tower body in a tangent form.
[0009] Furthermore: the outer surface of the tower body is also provided with a liquid inlet connected to the liquid storage chamber, and the liquid inlet is provided with a sealable sealing cover.
[0010] Furthermore: an exhaust port connected to the processing chamber is opened on the top of the tower body.
[0011] Furthermore: a liquid discharge port connected to the liquid storage chamber is installed at the bottom of the tower body, and a valve is installed on the liquid discharge port.
[0012] Beneficial effects of the utility model:
[0013] The utility model has spiral blades installed on the cylinder body, which play a role of blocking the flue gas, so that the flue gas in the treatment chamber can only flow upward in a spiral manner along the spiral blades, which can increase the residence time of the flue gas in the tower body, so that the desulfurization liquid sprayed by the nozzle can fully contact the flue gas, thereby improving the reaction effect between the flue gas and the desulfurization liquid, and improving the effect of flue gas desulfurization.
[0014] The utility model is provided with a plurality of air holes on the partition, and the desulfurization liquid sprayed from the nozzle can flow downward along the spiral sheet to the partition, and the desulfurization liquid on the partition can pass through the liquid flow holes and flow into the liquid storage chamber again for secondary utilization, thereby reducing the waste of desulfurization liquid. BRIEF DESCRIPTION OF THE DRAWINGS
[0015] Figure 1 It is a three-dimensional schematic diagram of the utility model;
[0016] Figure 2 It is a cross-sectional schematic diagram of the utility model;
[0017] Figure 3 It is a schematic diagram of the cross-sectional structure of the cylinder in the utility model.
[0018] The names corresponding to the marks in the figure are:
[0019] 1. Tower body; 2. Processing chamber; 3. Liquid storage chamber; 4. Cylinder; 5. Spiral blade; 6. Water pump; 7. Liquid extraction pipe; 8. Liquid spray pipe; 9. Nozzle; 10. Partition; 11. Liquid flow hole; 12. Smoke inlet pipe; 13. Liquid inlet; 14. Exhaust port; 15. Liquid discharge port; 16. Valve; 17. Support leg. DETAILED DESCRIPTION
[0020] The following will be combined with the drawings in the embodiments of the utility model to clearly and completely describe the technical solutions in the embodiments of the utility model. Obviously, the described embodiments are only part of the embodiments of the utility model, not all of the embodiments. Based on the embodiments in the utility model, all other embodiments obtained by ordinary technicians in this field belong to the scope of protection of the utility model.
[0021] Embodiments of the present utility model:
[0022] A dust removal device for a flue gas desulfurization tower comprises a tower body 1. A plurality of supporting legs 17 are fixed to the bottom of the tower body 1 at equal intervals in a circumferential direction. The supporting legs 17 are arranged to support the tower body 1. A partition 10 is fixed to the lower part of the tower body 1. The partition 10 divides the interior of the tower body 1 into a processing chamber 2 and a liquid storage chamber 3. The liquid storage chamber 3 is located at the lower part of the processing chamber 2. The flue gas can be desulfurized by the arrangement of the processing chamber 2. The desulfurization liquid can be stored by the arrangement of the liquid storage chamber 3. It should be noted that a desulfurizer is mixed with water to form a desulfurization liquid. A plurality of liquid flow holes 11 are provided on the partition 10. The desulfurization liquid after spraying can fall into the liquid storage chamber 3 again by the arrangement of the liquid flow holes 11. The desulfurization liquid can be used twice or multiple times, thereby reducing the waste of the desulfurization liquid.
[0023] A smoke inlet pipe 12 is fixed on the outer surface of the tower body 1 in a tangential manner, and the entrance end of the smoke inlet pipe 12 is connected to the interior of the processing chamber 2, so that after the smoke enters the processing chamber 2, it can flow along the inner wall of the tower body 1 to the position of the spiral sheet 5. An exhaust port 14 connected to the processing chamber 2 is fixed on the top of the tower body 1. Through the setting of the exhaust port 14, the treated smoke in the tower body 1 can be discharged.
[0024] A liquid inlet 13 is fixed at the lower part of the outer surface of the tower body 1, and one end of the liquid inlet 13 is connected to the interior of the liquid storage chamber 3. Through the setting of the liquid inlet 13, desulfurization liquid can be added to the liquid storage chamber 3. A liquid discharge port 15 is fixed at the center of the bottom of the tower body 1, and the top of the liquid discharge port 15 is connected to the liquid storage chamber 3. Through the setting of the liquid discharge port 15, the used desulfurization liquid in the liquid storage chamber 3 can be discharged. A valve 16 is installed on the liquid discharge port 15. Through the setting of the valve 16, the liquid discharge port 15 is closed or opened.
[0025] A cylinder 4 is fixed at the center of the top of the partition 10, and a water pump 6 is installed inside the cylinder 4. The water pump 6 is arranged to extract the desulfurized liquid. A liquid extraction pipe 7 is installed at the water extraction end of the water pump 6, and the bottom end of the liquid extraction pipe 7 passes through the partition 10 and extends to the lower part of the liquid storage chamber 3. A spiral liquid injection pipe 8 is installed at the output end of the water pump 6. Several nozzles 9 are fixed at equal intervals on the outer surface of the liquid injection pipe 8, and the spraying end of the nozzle 9 extends to the outside of the cylinder 4 and is located inside the tower body 1.
[0026] When desulfurizing flue gas, first connect the external flue gas pipeline with the smoke inlet pipe 12, and the untreated flue gas enters the tower body 1 through the smoke inlet pipe 12. After the untreated flue gas enters the tower body 1, it can flow upward in a spiral manner along the spiral blade 5.
[0027] Then start the water pump 6, and the output end of the water pump 6 extracts the desulfurization liquid in the liquid storage chamber 3 through the liquid extraction pipe 7. The extracted desulfurization liquid enters the liquid spray pipe 8 through the water pump 6. The desulfurization liquid in the liquid spray pipe 8 is sprayed to the outside of the cylinder 4 and located inside the tower body 1 through a plurality of nozzles 9. The desulfurization liquid after spraying is fully in contact with the untreated flue gas, thereby generating a chemical reaction, and desulfurizing the untreated flue gas. The treated flue gas is discharged through the exhaust port 14, and the desulfurization liquid after spraying can flow downward along the spiral sheet 5 to the partition 10, so that the desulfurization liquid on the partition 10 flows again to the liquid storage chamber 3 through the liquid flow hole 11 for multiple utilization.
Claims
1. A dust removal device for a flue gas desulfurization tower, comprising a tower body (1), wherein a processing chamber (2) and a liquid storage chamber (3) are sequentially arranged inside the tower body (1) from top to bottom, characterized in that: A barrel (4) is installed inside the treatment chamber (2), a spiral blade (5) is installed on the outer surface of the barrel (4), a water pump (6) is installed inside the barrel (4), a liquid suction pipe (7) extending into the liquid storage chamber (3) is installed at the water pumping end of the water pump (6), a spiral liquid spraying pipe (8) is installed at the water outlet end of the water pump (6), and a plurality of spray heads (9) extending to the outside of the barrel (4) are installed on the outer surface of the liquid spraying pipe (8).
2. The dust removal equipment for a flue gas desulfurization tower according to claim 1, characterized in that: A partition (10) is provided between the processing chamber (2) and the liquid storage chamber (3), and a plurality of liquid flow holes (11) are provided on the partition (10), and the plurality of liquid flow holes (11) are located outside the cylinder (4).
3. The dust removal equipment for a flue gas desulfurization tower according to claim 1, characterized in that: A smoke inlet pipe (12) communicating with the interior of the processing chamber (2) is installed on the outer surface of the tower body (1), and one end of the smoke inlet pipe (12) is fixedly connected to the outer surface of the tower body (1) in a tangential manner.
4. The dust removal equipment for a flue gas desulfurization tower according to claim 1, characterized in that: The outer surface of the tower body (1) is also provided with a liquid inlet (13) which is in communication with the liquid storage chamber (3), and the liquid inlet (13) is provided with a detachable sealing cover.
5. The dust removal equipment for a flue gas desulfurization tower according to claim 1, characterized in that: An exhaust port (14) communicating with the processing chamber (2) is provided at the top of the tower body (1).
6. The dust removal equipment for a flue gas desulfurization tower according to claim 1, characterized in that: The bottom of the tower body (1) is provided with a liquid discharge port (15) which is in communication with the liquid storage chamber (3), and a valve (16) is installed on the liquid discharge port (15).