Semi-dry flue gas desulfurization device based on rotary spraying

Abstract

The utility model discloses a semi-dry flue gas desulfurization device based on rotary spraying, and relates to the field of desulfurization devices. The semi-dry flue gas desulfurization device based on rotary spraying comprises a spraying purification tower main body, a gas outlet pipe is arranged above the spraying purification tower main body, a drying mechanism is arranged outside the spraying purification tower main body, and the drying mechanism comprises a drying treatment box which is mounted at the end part of the gas outlet pipe; the drying particle storage net box is arranged in the drying treatment box, drying particles are arranged in the drying particle storage net box and used for adsorbing gas moisture, and the rotating plate is rotationally arranged above the drying particle storage net box. According to the semi-dry flue gas desulfurization device based on rotary spraying, gas is quickly dispersed by using the rotary plate, and meanwhile, the gas dispersion area is increased, so that water vapor is dried in cooperation with drying particles in the drying particle storage net box, and finally, the drying net plate is used for further drying, so that flue gas is dried; therefore, the next step of drying treatment is facilitated.

Description

Technical Field

[0001] The utility model relates to the technical field of desulfurization devices, in particular to a flue gas desulfurization device based on a rotary spray semi-dry type. Background Art

[0002] With the development of modern industry, a large amount of sulfur-containing flue gas will be produced. In order to make the flue gas meet the emission standards, a spray desulfurization device, also called a spray tower, is required. The sulfur substances in the flue gas are treated using a spray tower-type rotating spray device to dissolve the sulfur in the water.

[0003] The existing spray tower has the problem that the water vapor produced by purifying sulfur substances will affect the flue gas purification treatment results;

[0004] The reason for this problem is that the principle used by the spray tower is to use a rotating spray device in the spray tower to atomize water, so as to mix water with flue gas, and the water vapor will blend with the sulfur substances in the flue gas, thereby purifying the sulfur substances in the exhaust gas. During the desulfurization purification process, a large number of water molecules will remain in the flue gas, and the water molecules will be discharged from the spray tower along the outlet pipe. At this time, some sulfur substances will be discharged from the spray tower together with the water vapor and the flue gas. At the same time, the flue gas needs to undergo the next purification process after treating the sulfur substances. If a large number of water molecules enter the next purification process together with the flue gas, it will cause secondary pollution to the next purification process. Therefore, we propose a flue gas desulfurization device based on rotary spray semi-dry type. Utility Model Content

[0005] In view of the deficiencies in the prior art, the utility model provides a flue gas desulfurization device based on rotary spray semi-dry type, which solves the problem that the water vapor generated by the existing spray tower for purifying sulfur substances will affect the flue gas purification treatment results.

[0006] To achieve the above objectives, the utility model is implemented through the following technical solutions: a flue gas desulfurization device based on rotary spray semi-dry type, comprising a spray purification tower body, an air outlet pipe is arranged above the spray purification tower body, a drying mechanism is arranged outside the spray purification tower body, the drying mechanism comprises a drying treatment box, which is installed at the end of the air outlet pipe, the drying treatment box is used to dry the exhaust gas, a dry particle storage mesh box is arranged inside the drying treatment box, dry particles are arranged inside the dry particle storage mesh box, the dry particles are used to absorb gas moisture, a rotating plate is rotatably arranged above the dry particle storage mesh box, and the rotating plate is used to disperse the gas.

[0007] Preferably, a gas impurity purification box is provided on the side of the spray purification tower body.

[0008] Preferably, the interior of the drying treatment box is fixedly connected with an installation box, and the dry particle storage net box is arranged inside the installation box.

[0009] Preferably, a support rod is fixedly connected to the interior of the drying treatment box, a drying mesh plate is sleeved on the exterior of the support rod, and the drying mesh plate is arranged below the installation box, and the drying mesh plate is arranged below the dry particle storage mesh box.

[0010] Preferably, a function box is fixedly connected to the top end of the support rod, and a rotation driver is installed inside the function box.

[0011] Preferably, a support frame is provided outside the rotary driver, and the support frame is fixedly connected to the inside of the functional box.

[0012] Preferably, a rotating disk is fixedly connected to the outer surface of the output end of the rotating driver, a rotating rod is fixedly connected to the upper back surface of the rotating disk, the rotating plate is sleeved on the outside of the rotating rod, and a connecting pipe is provided on the side of the drying treatment box.

[0013] The utility model discloses a flue gas desulfurization device based on a rotary spray semi-dry type, which has the following beneficial effects: the flue gas desulfurization device based on a rotary spray semi-dry type processes the flue gas through a spray purification tower body, and the purified flue gas and part of the water vapor enter the interior of a drying treatment box from the position of an exhaust pipe, and the gas is dispersed to the surrounding positions of the drying treatment box by the rotation of a rotating plate, and dry particles are placed inside a dry particle storage mesh box, and the dry particles can dry the moisture in the gas, and then the drying mesh plate will quickly absorb excess water vapor, so as to further dry the gas, and by setting a drying treatment box, the rotary plate is used to quickly disperse the gas and increase the gas dispersion area at the same time, so as to cooperate with the dry particles in the dry particle storage mesh box to dry the water vapor, and finally the drying mesh plate is used for further drying, so that the flue gas is dry, so as to facilitate the next step of drying treatment. BRIEF DESCRIPTION OF THE DRAWINGS

[0014] In order to more clearly illustrate the embodiments of the utility model or the technical solutions in the prior art, the drawings required for use in the embodiments or the description of the prior art will be briefly introduced below. Obviously, the drawings described below are only some embodiments of the utility model. For ordinary technicians in this field, other drawings can be obtained based on these drawings without paying creative work.

[0015] Figure 1 It is a schematic diagram of the overall structure of the utility model;

[0016] Figure 2 This is one of the schematic diagrams of the structure of the drying treatment box of the utility model;

[0017] Figure 3 This is a schematic diagram of the structure of the net box for storing dry particles of the utility model;

[0018] Figure 4 This is the second schematic diagram of the structure of the drying treatment box of the utility model;

[0019] Figure 5 This is a schematic diagram of the structure of the rotating rod and the rotating plate of the utility model.

[0020] In the figure: 1. spray purification tower body; 101. gas impurity purification box; 102. air outlet pipe; 2. drying treatment box; 201. installation box; 202. rotating plate; 203. support frame; 204. function box; 205. dry particle storage net box; 206. drying net plate; 207. connecting pipe; 208. support rod; 209. rotating drive; 210. rotating rod; 211. rotating disk. DETAILED DESCRIPTION

[0021] In order to make the purpose, technical solution and advantages of the embodiments of the utility model clearer, the technical solution in the embodiments of the utility model is described clearly and completely. Obviously, the described embodiments are part of the embodiments of the utility model, not all of the embodiments. Based on the embodiments of the utility model, all other embodiments obtained by ordinary technicians in this field without creative work are within the scope of protection of the utility model.

[0022] The embodiment of the present application provides a flue gas desulfurization device based on rotary spray semi-dry type, which solves the problem that the water vapor generated by the existing spray tower for purifying sulfur substances will affect the flue gas purification treatment results.

[0023] In order to better understand the above technical solution, the above technical solution will be described in detail below in conjunction with the accompanying drawings and specific implementation methods.

[0024] The utility model embodiment discloses a flue gas desulfurization device based on a rotary spray semi-dry type.

[0025] According to the attached Figure 1-5 As shown, it includes a spray purification tower body 1, and the spray purification tower body 1 can refer to the spray purification machine with model FH-XDII. An air outlet pipe 102 is arranged above the spray purification tower body 1, and a drying mechanism is arranged outside the spray purification tower body 1. The drying mechanism includes a drying treatment box 2, which is installed at the end of the air outlet pipe 102. The drying treatment box 2 is used for drying the exhaust gas. A dry particle storage net box 205 is arranged inside the drying treatment box 2. Dry particles are arranged inside the dry particle storage net box 205. The dry particles are used to absorb moisture in the gas. A rotating plate 202 is rotatably arranged above the dry particle storage net box 205, and the rotating plate 202 is used to disperse the gas.

[0026] The flue gas undergoes preliminary impurity purification from the inside of the gas impurity purification box 101, and then enters the inside of the spray purification tower body 1 from the gas impurity purification box 101. The water mist generated by the rotating spray device inside the spray purification tower body 1 is mixed with the flue gas. At this time, the sulfur substances in the flue gas will be mixed with water, and the water will be desulfurized and purified.

[0027] The flue gas is treated by the spray purification tower body 1. The purified flue gas and part of the water vapor enter the drying treatment box 2 from the position of the exhaust pipe 102. At this time, the rotary driver 209 will drive the rotating plate 202 to rotate. The rotating plate 202 rotates to disperse the gas to the surrounding positions of the drying treatment box 2, and enter the position of the dry particle storage net box 205 from the surrounding positions of the drying treatment box 2. Dry particles are placed inside the dry particle storage net box 205. The dry particles dry the moisture in the gas. Then the gas will enter the inside of the drying net plate 206. The inside of the drying net plate 206 is provided with drying material to quickly absorb excess water vapor, thereby further drying the gas.

[0028] A gas impurity purification box 101 is arranged on the side of the spray purification tower body 1, an installation box 201 is fixedly connected to the interior of the drying treatment box 2, a dry particle storage net box 205 is arranged inside the installation box 201, a support rod 208 is fixedly connected to the interior of the drying treatment box 2, a drying net plate 206 is sleeved on the outside of the support rod 208, and the drying net plate 206 is arranged below the installation box 201, and the drying net plate 206 is arranged below the dry particle storage net box 205.

[0029] By setting up a drying treatment box 2, a rotating plate 202 is used to quickly disperse the gas and increase the gas dispersion area, so as to cooperate with the dry particles inside the dry particle storage net box 205 to dry the water vapor, and finally a drying net plate 206 is used for further drying to dry the flue gas, thereby facilitating the next drying process.

[0030] The top of the support rod 208 is fixedly connected to the function box 204, a rotating driver 209 is installed inside the function box 204, a support frame 203 is arranged outside the rotating driver 209, the support frame 203 is fixedly connected to the inside of the function box 204, a rotating disk 211 is fixedly connected to the outer surface of the output end of the rotating driver 209, a rotating rod 210 is fixedly connected to the upper back side of the rotating disk 211, the rotating plate 202 is sleeved on the outside of the rotating rod 210, and a connecting pipe 207 is arranged on the side of the drying treatment box 2.

[0031] The rotary driver 209 is a rotary driving device that can drive the rotary disk 211 to rotate inside the function box 204, thereby driving the rotary plate 202 to rotate. During the rotation of the rotary plate 202, an outward airflow is generated, thereby driving the gas to the surroundings of the drying treatment box 2, thereby dispersing the gas.

[0032] In summary, compared with the prior art, the present invention has the following beneficial effects:

[0033] The flue gas is treated by the spray purification tower body 1. The purified flue gas and part of the water vapor enter the drying treatment box 2 from the position of the exhaust pipe 102. The rotating plate 202 rotates to disperse the gas to the surrounding positions of the drying treatment box 2. Dry particles are placed inside the dry particle storage net box 205. The dry particles can dry the moisture in the gas. Then the drying net plate 206 will quickly absorb the excess water vapor to further dry the gas. The rotating plate 202 is used to quickly disperse the gas and increase the gas dispersion area at the same time, so as to cooperate with the dry particles in the dry particle storage net box 205 to dry the water vapor. Finally, the drying net plate 206 is used for further drying to dry the flue gas, thereby facilitating the next drying process.

[0034] The above shows and describes the basic principle and main features of the utility model and the advantages of the utility model. Those skilled in the art should understand that the utility model is not limited by the above embodiments. The above embodiments and descriptions are only for explaining the principle of the utility model. Without departing from the spirit and scope of the utility model, the utility model may have various changes and improvements, which fall within the scope of the utility model to be protected. The scope of protection claimed by the utility model is defined by the attached claims and their equivalents.

Claims

1. A flue gas desulfurization device based on a rotary spray semi-dry type, comprising a spray purification tower body (1), wherein an air outlet pipe (102) is arranged above the spray purification tower body (1), characterized in that: A drying mechanism is arranged outside the spray purification tower body (1), and the drying mechanism comprises: A drying treatment box (2) is installed at the end of the gas outlet pipe (102), and the drying treatment box (2) is used to dry the exhaust gas; A dry particle storage net box (205) is arranged inside the drying treatment box (2), and dry particles are arranged inside the dry particle storage net box (205), and the dry particles are used to absorb gas moisture; A rotating plate (202) is rotatably disposed above a dry particle storage net box (205), and the rotating plate (202) is used to disperse gas.

2. A rotary spray semi-dry flue gas desulfurization device according to claim 1, characterized in that: A gas impurity purification box (101) is provided on the side of the spray purification tower body (1).

3. A rotary spray semi-dry flue gas desulfurization device according to claim 1, characterized in that: The interior of the drying treatment box (2) is fixedly connected to a mounting box (201), and the dry particle storage net box (205) is arranged inside the mounting box (201).

4. A flue gas desulfurization device based on rotary spray semi-dry type according to claim 1, characterized in that: A support rod (208) is fixedly connected to the interior of the drying treatment box (2), a drying mesh plate (206) is sleeved on the exterior of the support rod (208), and the drying mesh plate (206) is arranged below the installation box (201), and the drying mesh plate (206) is arranged below the dry particle storage mesh box (205).

5. A rotary spray semi-dry flue gas desulfurization device according to claim 4, characterized in that: The top end of the support rod (208) is fixedly connected to a function box (204), and a rotation driver (209) is installed inside the function box (204).

6. A rotary spray semi-dry flue gas desulfurization device according to claim 5, characterized in that: A support frame (203) is arranged outside the rotary driver (209), and the support frame (203) is fixedly connected to the inside of the function box (204).

7. A rotary spray semi-dry flue gas desulfurization device according to claim 6, characterized in that: The outer surface of the output end of the rotary driver (209) is fixedly connected to a rotary disk (211), the upper back surface of the rotary disk (211) is fixedly connected to a rotary rod (210), the rotating plate (202) is sleeved on the outside of the rotary rod (210), and a connecting pipe (207) is provided on the side of the drying treatment box (2).

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