Combined desulfurization device based on flue gas spraying rotational flow

Abstract

The utility model discloses a combined type desulfurization device based on flue gas spraying and rotational flow, relates to the technical field of desulfurization device structures, and aims to solve the problems that the existing desulfurization device is poor in desulfurization effect, so that the treatment effect on flue gas is poor, and the environment is easily polluted when the flue gas is discharged. A gas inlet seat is arranged below one end of the outer wall of the desulfurizing tower, a gas outlet seat is arranged at the upper end of the desulfurizing tower, a supporting base is arranged below the desulfurizing tower, a water drainage seat is arranged at one end of the supporting base, a water inlet seat is arranged above one end of the outer wall of the desulfurizing tower, and a connecting pipeline is arranged in the desulfurizing tower. A spraying device is installed on one side of the connecting pipeline, a nozzle is installed below the spraying device, a supporting seat is installed below the spraying device, a water drainage opening is formed in the supporting seat, a water drainage pipe is installed below the supporting seat, and a rotational flow device is arranged at the upper end of the supporting seat.

Description

Technical Field

[0001] This utility model relates to the field of desulfurization device structure technology, and in particular to a desulfurization device based on flue gas spray cyclone combination. Background Technology

[0002] A desulfurization unit is a device used to reduce the emission of sulfur oxides in industrial waste gas. Its main purpose is to convert sulfur dioxide in waste gas into harmless substances through chemical reactions, thereby reducing pollution to the atmosphere, soil and water and protecting the ecological environment.

[0003] A search revealed that authorization announcement number CN213408216U discloses a spray cyclone combined desulfurization device, belonging to the field of flue gas desulfurization technology. This spray cyclone combined desulfurization device includes a spray tower shell, an air filter fixedly connected to the top of the inner side of the spray tower shell, a dehumidifier fixedly connected to the bottom of the air filter, and an atomizing nozzle embedded in the inner wall of the spray tower shell near the bottom of the dehumidifier. One end of the atomizing nozzle is embedded and connected to a water pipe, and the other end of the water pipe is embedded and connected to a water pump. One end of the water pump is fixedly connected to a water tank. In this invention, there are several atomizing nozzles arranged in a ring. When a fan delivers air into the shell through pipe two, the water pump draws sodium hydroxide solution from the sodium hydroxide solution tank through the water pipe, and then sprays the sodium hydroxide solution from the atomizing nozzles, thus desulfurizing the air during delivery. Furthermore, the sodium hydroxide solution is sprayed more evenly, achieving a better desulfurization effect.

[0004] However, the existing desulfurization devices have poor desulfurization effects, resulting in poor treatment of flue gas and easy pollution of the surrounding environment when the flue gas is emitted. Therefore, there is an urgent need in the market for a flue gas spray cyclone combined desulfurization device to solve these problems. Utility Model Content

[0005] The purpose of this utility model is to provide a flue gas spray cyclone combined desulfurization device to solve the problem mentioned in the background art that the existing desulfurization devices have poor desulfurization effect, resulting in poor flue gas treatment effect and easy pollution of the surrounding environment when the flue gas is emitted.

[0006] To achieve the above objectives, the present invention provides the following technical solution:

[0007] A flue gas spray cyclone combined desulfurization device includes a desulfurization tower, with protective seats arranged around the outer wall of the desulfurization tower, an air inlet seat arranged below one end of the outer wall of the desulfurization tower, an air outlet seat arranged at the upper end of the desulfurization tower, a support base arranged below the desulfurization tower, a drain seat arranged at one end of the support base, a water inlet seat arranged above one end of the outer wall of the desulfurization tower, a connecting pipe arranged inside the desulfurization tower, a spraying device installed on one side of the connecting pipe, a nozzle installed below the spraying device, a support base installed below the spraying device, a drain outlet arranged inside the support base, a drain pipe installed below the support base, and a cyclone device arranged at the upper end of the support base.

[0008] By adopting the above technical solutions, the desulfurization tower can better desulfurize the flue gas, thereby improving the desulfurization effect of the flue gas.

[0009] Furthermore, six protective seats are provided, which are distributed sequentially around the outer wall of the desulfurization tower, and the protective seats and the desulfurization tower are an integral structure.

[0010] By adopting the above technical solution, the structure between the protective seat and the desulfurization tower can be made more robust, and the protective seat can effectively protect the desulfurization tower.

[0011] Furthermore, the support base is welded to the desulfurization tower, and reinforcing ribs are provided around the outer wall of the support base. The reinforcing ribs are welded to the support base, and a drainage seat is provided at one end of the support base.

[0012] By adopting the above technical solution, the structural strength of the support base can be improved by setting the reinforcing ribs, and the drainage seat can be used to conveniently discharge and treat the desulfurized wastewater.

[0013] Furthermore, the connecting pipe is provided correspondingly to the water inlet seat, and the water inlet seat is connected to the connecting pipe.

[0014] By adopting the above technical solution, the treatment liquid can be easily introduced through the water inlet seat, thereby effectively desulfurizing the flue gas.

[0015] Furthermore, the lower end of the spraying device is provided with a mounting base, and the nozzle is correspondingly provided with the mounting base, and the nozzle and the mounting base are connected by a thread.

[0016] By adopting the above technical solution, the nozzle and the mounting base can be easily connected and installed. The installed nozzle can easily spray out liquid, so that the liquid can react well with the flue gas, thereby improving the desulfurization effect.

[0017] Furthermore, four drain pipes are provided, and the drain pipes are connected to the drain outlets.

[0018] By adopting the above technical solution, the wastewater after desulfurization can be conveniently discharged and treated.

[0019] Furthermore, a swirl plate is installed inside the swirl device, and the swirl plate is welded to the swirl device.

[0020] By adopting the above technical solution, the flue gas can generate strong centrifugal rotation and fully contact the liquid in the tower, thereby improving the gas-liquid two-phase mass transfer efficiency and thus improving the desulfurization effect of the flue gas.

[0021] Compared with the prior art, the beneficial effects of this utility model are:

[0022] (1) This utility model introduces waste gas through the inlet seat, then the waste gas enters the interior of the desulfurization tower, and then introduces liquid through the water inlet seat, then the liquid enters the interior of the connecting pipe, and then sprays it out through the nozzle. This allows the liquid to react with the waste gas, thereby desulfurizing the waste gas. Then the wastewater after the reaction can be discharged through the drain seat to avoid polluting the surrounding environment.

[0023] (2) The swirl device installed in this utility model enables the flue gas to generate strong centrifugal rotation when passing through the swirl plate, and fully contact the liquid in the tower, thereby improving the gas-liquid two-phase mass transfer efficiency and thus improving the desulfurization effect of the flue gas. The drain outlet and drain pipe set up enable the liquid to flow conveniently, and the liquid passing through the drain pipe can react with the waste gas in the lower layer, thereby making desulfurization more convenient and effectively improving the desulfurization efficiency. Attached Figure Description

[0024] Figure 1 This is a perspective view of the entire utility model;

[0025] Figure 2 This is an overall sectional view of the present invention;

[0026] Figure 3 This is a top view of the vortex device of this utility model;

[0027] Figure 4 For the present utility model Figure 2 A magnified view of a portion of area A.

[0028] In the diagram: 1. Desulfurization tower; 101. Inlet seat; 102. Outlet seat; 2. Protective seat; 3. Support base; 301. Reinforcing rib; 302. Drain seat; 4. Water inlet seat; 5. Connecting pipe; 6. Spraying device; 601. Mounting seat; 7. Nozzle; 8. Support seat; 801. Drain outlet; 9. Swirl device; 10. Swirl plate; 11. Drain pipe. Detailed Implementation

[0029] The technical solutions of the present utility model will be clearly and completely described below with reference to the accompanying drawings of the embodiments of the present utility model. Obviously, the described embodiments are only some embodiments of the present utility model, and not all embodiments.

[0030] Please see Figures 1-4This utility model provides an embodiment of a flue gas spray cyclone combined desulfurization device, including a desulfurization tower 1. Six protective seats 2 are arranged around the outer wall of the desulfurization tower 1, distributed sequentially around its perimeter. The protective seats 2 and the desulfurization tower 1 are integrally formed. An air inlet seat 101 is located below one end of the outer wall of the desulfurization tower 1, and an air outlet seat 102 is located at the upper end of the desulfurization tower 1. A support base 3 is located below the desulfurization tower 1, and a drain seat 302 is located at one end of the support base 3. A drainage seat 302 is located above one end of the outer wall of the desulfurization tower 1. The desulfurization tower 1 has an internal connecting pipe 5, which corresponds to the water inlet seat 4 and is connected to it. A spraying device 6 is installed on one side of the connecting pipe 5, and a nozzle 7 is installed below the spraying device 6. A mounting base 601 is installed at the lower end of the spraying device 6, and the nozzle 7 corresponds to the mounting base 601. The nozzle 7 and mounting base 601 are connected by threads. A support base 8 is installed below the spraying device 6, and a drain outlet 801 is installed inside the support base 8. A drain pipe 11 is installed below the support base 8 for drainage. Four pipes 11 are provided. The drain pipes 11 are connected to the drain outlets 801. A swirling device 9 is provided at the upper end of the support base 8. A swirling plate 10 is installed inside the swirling device 9 and welded to it. The protective seat 2 enhances the protection of the desulfurization tower 1. The support base 3 supports the desulfurization tower 1. The drain seat 302 facilitates wastewater discharge. The spraying device sprays liquid, thus facilitating flue gas desulfurization. The swirling device 9 enables… When the flue gas passes through the swirl plate 10, it generates a strong centrifugal rotation motion, which fully contacts the liquid in the tower, thereby improving the gas-liquid two-phase mass transfer efficiency and thus improving the desulfurization effect of the flue gas. The drain port 801 and drain pipe 11 allow the liquid to flow easily, and the liquid passing through the drain pipe 11 can react with the lower layer of flue gas to achieve desulfurization. It should be noted that, in order to save space and highlight the innovative elements of this patent, such as the working principle and process of how the liquid reacts with the flue gas, this patent will not elaborate on them.

[0031] See Figure 1 and Figure 2 The support base 3 is welded to the desulfurization tower 1. The outer wall of the support base 3 is provided with reinforcing ribs 301 around its perimeter. The reinforcing ribs 301 are welded to the support base 3. One end of the support base 3 is provided with a drainage seat 302. The reinforcing ribs 301 can improve the structural strength of the support base 3. The drainage seat 302 can facilitate the discharge of desulfurized wastewater, thereby facilitating wastewater treatment.

[0032] Working principle: During use, waste gas is introduced through the inlet seat 101 and then enters the interior of the desulfurization tower 1. Liquid is introduced through the water inlet seat 4 and then enters the interior of the connecting pipe 5. It is then sprayed out through the nozzle 7, allowing the liquid to react with the waste gas, thereby desulfurizing the waste gas. The wastewater after the reaction is discharged through the drain seat 302 to avoid pollution to the surrounding environment. The installed swirl device 9 causes the flue gas to generate a strong centrifugal rotation when passing through the swirl plate 10, which fully contacts the liquid in the tower, thereby improving the gas-liquid two-phase mass transfer efficiency and thus improving the desulfurization effect of the flue gas. The set drain port 801 and drain pipe 11 allow the liquid to flow easily, and the liquid passing through the drain pipe 11 can react with the waste gas in the lower layer, thereby facilitating desulfurization and effectively improving the desulfurization efficiency.

[0033] It will be apparent to those skilled in the art that this invention is not limited to the details of the exemplary embodiments described above, and that it can be implemented in other specific forms without departing from the spirit or essential characteristics of this invention. Therefore, the embodiments should be considered illustrative and non-limiting in all respects, and the scope of this invention is defined by the appended claims rather than the foregoing description. Thus, it is intended that all variations falling within the meaning and scope of equivalents of the claims be included within this invention. No reference numerals in the claims should be construed as limiting the scope of the claims.

Claims

1. A flue gas spray cyclone combined desulfurization device, comprising a desulfurization tower (1), characterized in that: The desulfurization tower (1) is provided with protective seats (2) around its outer wall. An air inlet seat (101) is provided below one end of the outer wall of the desulfurization tower (1). An air outlet seat (102) is provided at the upper end of the desulfurization tower (1). A support base (3) is provided below the desulfurization tower (1). A drain seat (302) is provided at one end of the support base (3). A water inlet seat (4) is provided above one end of the outer wall of the desulfurization tower (1). A connecting pipe (5) is provided inside the desulfurization tower (1). A spraying device (6) is installed on one side of the connecting pipe (5). A nozzle (7) is installed below the spraying device (6). A support seat (8) is installed below the spraying device (6). A drain outlet (801) is provided inside the support seat (8). A drain pipe (11) is installed below the support seat (8). A swirling device (9) is provided at the upper end of the support seat (8).

2. The flue gas spray cyclone combined desulfurization device according to claim 1, characterized in that: There are six protective seats (2), which are distributed around the outer wall of the desulfurization tower (1). The protective seats (2) and the desulfurization tower (1) are an integral structure.

3. The flue gas spray cyclone combined desulfurization device according to claim 2, characterized in that: The support base (3) is welded to the desulfurization tower (1). The outer wall of the support base (3) is provided with reinforcing ribs (301) around its perimeter. The reinforcing ribs (301) are welded to the support base (3). One end of the support base (3) is provided with a drainage seat (302).

4. The flue gas spray cyclone combined desulfurization device according to claim 3, characterized in that: The connecting pipe (5) is provided corresponding to the water inlet seat (4), and the water inlet seat (4) is connected to the connecting pipe (5).

5. A flue gas spray cyclone combined desulfurization device according to claim 4, characterized in that: The lower end of the spraying device (6) is provided with a mounting base (601), and the nozzle (7) is provided correspondingly to the mounting base (601). The nozzle (7) and the mounting base (601) are connected by a thread.

6. A flue gas spray cyclone combined desulfurization device according to claim 5, characterized in that: Four drain pipes (11) are provided, and the drain pipes (11) are connected to the drain outlets (801).

7. A flue gas spray cyclone combined desulfurization device according to claim 6, characterized in that: The swirling device (9) has a swirling plate (10) installed inside, and the swirling plate (10) is welded to the swirling device (9).

Images