Waste gas treatment device for electronic detonator production

By installing spiral guides and molecular sieves inside the waste gas treatment tower, the problems of short waste gas residence time and uneven mixing are solved, achieving a more efficient waste gas treatment effect.

CN223668959UActive Publication Date: 2025-12-16SHANXI HUHUA GRP
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Patent Information

Application Number
CN202423232870.X
Authority / Receiving Office
CN · China
Patent Type
Utility models(China)
Current Assignee / Owner
Filing Date
2024-12-26
Publication Date
2025-12-16
Estimated Expiration
2034-12-26

AI Technical Summary

Technical Problem

Existing waste gas treatment towers in electronic detonator production suffer from problems such as short waste gas residence time and uneven mixing, resulting in insufficient reaction and poor treatment effect.

Method used

A spiral guide is installed inside the treatment tower to form a cyclone, which, combined with a molecular sieve, improves the contact effect between the waste gas and the treatment liquid, thereby enhancing the treatment capacity.

Benefits of technology

By forming a cyclone through the spiral guide, the residence time of the exhaust gas in the tower is extended, improving the uniformity and treatment effect of the exhaust gas and enhancing the exhaust gas treatment capacity.

✦ Generated by Eureka AI based on patent content.

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Abstract

The utility model relates to the technical field of waste gas treatment devices, and discloses a waste gas treatment device for electronic detonator production, which comprises a treatment tower, an air inlet pipe is connected to the bottom of the treatment tower, an air outlet pipe is connected to the top of the treatment tower, the air inlet pipe and the air outlet pipe are respectively provided with an air valve, and waste gas enters the treatment tower through the air inlet pipe and leaves through the air outlet pipe after being treated; a water tank and a replacement structure; the water tank is arranged on the front side of the treatment tower, the replacement structure is arranged on the water tank, and the water tank replaces water in the treatment tower through the replacement structure; the spraying structure is arranged at the top of the treatment tower; the efficient reaction layer is arranged below the spraying structure, and the waste gas is in contact with the water body in the efficient reaction layer; the spiral flow guide part is arranged below the efficient reaction layer, and the waste gas forms cyclone through the spiral flow guide part. Compared with the prior art, the waste gas treatment device has the advantages that the spiral flow guide piece is arranged, waste gas can be guided through the spiral rising fan blade structure, cyclone is formed, and the waste gas treatment capacity is higher.
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Description

TECHNICAL FIELD

[0001] The utility model relates to waste gas treatment device technical field, specifically point to a kind of waste gas treatment device for electronic detonator production. BACKGROUND

[0002] Electronic detonator is a kind of electronic control mode is used to control the initiation process electric detonator, mainly by detonator, encoder and initiator, electronic detonator is widely used in industrial blasting, film shooting and other fields. In industrial blasting, electronic detonator can accurately control blasting time and energy, improve blasting efficiency and safety. In film shooting, electronic detonator is used to control the special effect of explosion scene. And in the production process of electronic detonator, a large amount of acid and alkali waste gas is generated, which needs to be treated by waste gas treatment tower.

[0003] The existing waste gas treatment tower on the market mostly provides negative pressure through the fan at the end to ensure the flow direction and flow rate of the internal waste gas, and sprays the waste gas, but in order to prevent the negative pressure value of the exhaust pipe in the workshop from being too low, causing the waste gas to diffuse in the workshop, the fan generally provides a large negative pressure, the internal wind speed of the treatment tower is fast, the residence time of the waste gas in the treatment tower is short, and the gas is not uniformly mixed, which is easy to cause insufficient reaction, affecting the treatment effect of the waste gas, and after discharge, causing harm to the environment. UTILITY MODEL CONTENT

[0004] The technical problem to be solved by the utility model is to overcome the above technical difficulties, and to provide a waste gas treatment device for electronic detonator production, which is provided with a spiral flow guide in the treatment tower, and the fan blade structure rising spirally guides the waste gas entering the treatment tower to form a cyclone, thereby improving the residence time and uniformity of the waste gas in the treatment tower, and improving the contact effect of the waste gas and the treatment liquid by molecular sieve to strengthen the treatment capacity.

[0005] To solve the above technical problems, the technical scheme provided by the utility model is:

[0006] A waste gas treatment device for electronic detonator production, comprising:

[0007] A treatment tower is connected with an air inlet pipe at the bottom and an air outlet pipe at the top, and the air inlet pipe and the air outlet pipe are respectively provided with air valves, the waste gas enters the treatment tower through the air inlet pipe, and leaves the treatment tower through the air outlet pipe after treatment;

[0008] A water tank and a replacement structure; the water tank is arranged on the front side of the treatment tower, and the replacement structure is arranged on the water tank; the water tank replaces the water in the treatment tower through the replacement structure;

[0009] A spraying structure is arranged on the top of the treatment tower;

[0010] The high-efficiency reaction layer is arranged below the spraying structure, and the waste gas contacts with the water body in the high-efficiency reaction layer.

[0011] The spiral flow guide member is arranged below the high-efficiency reaction layer, and the waste gas forms a cyclone through the spiral flow guide member.

[0012] As an improvement, the displacement structure comprises a water supplement pipe, a drainage pipe and a chemical adding pipe; a water inlet is reserved at the bottom of the rear side wall of the water tank, and the water tank is communicated with the inside of the treatment tower through the water inlet; the drainage pipe is connected with the bottom of the side wall of the water tank; the water supplement pipe and the chemical adding pipe are arranged on the left and right sides of the water tank respectively and are connected with the top wall of the water tank; and the water supplement pipe, the drainage pipe and the chemical adding pipe are respectively provided with water valves.

[0013] As an improvement, the spraying structure comprises a water pumping pipe, a high-pressure water pump, a filter, a water distribution pipe and a spray head; the high-pressure water pump is fixed on the top of the water tank, and the input end of the high-pressure water pump is connected with the bottom of the water tank through the water pumping pipe; the water distribution pipe is fixed in the treatment tower and is horizontally arranged on the top of the treatment tower; a plurality of spray heads are uniformly arranged on the water distribution pipe; the filter is a Y-shaped filter, and one end of the filter is connected with the output end pipeline of the high-pressure water pump, and the other end of the filter is connected with the water distribution pipe through a pipeline.

[0014] As an improvement, the spiral flow guide member is uniformly provided with a plurality of fan blade structures in the circumferential direction, and the fan blade structures are arranged in a spiral upward manner; the spiral flow guide member is fixed in the treatment tower and is arranged above the air inlet pipe.

[0015] As an improvement, the high-efficiency reaction layer comprises a sieve plate and a molecular sieve; the sieve plate is fixed in the treatment tower and is horizontally arranged below the water distribution pipe; and the molecular sieve is stacked on the sieve plate.

[0016] Compared with the prior art, the utility model has the advantages of:

[0017] 1. One layer of molecular sieve is arranged, the contact area of waste gas and treatment liquid can be increased, the treatment effect of waste gas is improved, and the utility model is more efficient.

[0018] 2. The spiral flow guide member is arranged, the spiral upward fan blade structure can guide the waste gas entering the treatment tower, a cyclone is formed, the residence time and uniformity of the waste gas in the treatment tower are improved, the waste gas treatment capacity is stronger, and the waste gas treatment effect is better. BRIEF DESCRIPTION OF DRAWINGS

[0019] Figure 1 is the structure diagram of the utility model Figure 1 .

[0020] Figure 2 is the structure diagram of the utility model Figure 2 .

[0021] Figure 3 is the sectional view of the water tank of the utility model.

[0022] Figure 4 It is the structure diagram of the spraying structure of the utility model.

[0023] Figure 5 It is the section view diagram of the processing tower of the utility model.

[0024] As shown in the figure: 1, processing tower, 2, water tank, 3, air inlet pipe, 4, air valve, 5, air outlet pipe, 6, window, 7, cover, 8, water inlet, 9, drain pipe, 10, water supply pipe, 11, dosing pipe, 12, water suction pipe, 13, high-pressure water pump, 14, filter, 15, water distribution pipe, 16, spray head, 17, sieve plate, 18, spiral flow guide. DETAILED DESCRIPTION

[0025] In the description of the utility model, it is understood that the orientation or positional relationship indicated by the terms "center", "transverse", "upper", "lower", "left", "right", "vertical", "horizontal", "top", "bottom", "inner", "outer" and the like is based on the orientation or positional relationship shown in the drawings, and is only for the convenience of describing the utility model and simplifying the description, and therefore cannot be understood as indicating or implying that the indicated device or element must have a particular orientation, be constructed and operated in a particular orientation, and therefore cannot be understood as a limitation on the utility model. In addition, the terms "first" and "second" are only for the purpose of description, and cannot be understood as indicating or implying relative importance or implicitly indicating the number of the indicated technical features. Therefore, the features limited by "first" and "second" can explicitly or implicitly include one or more of the features. In the description of the utility model, unless otherwise specified, the meaning of "a plurality of" is two or more. In addition, the term "includes" and any variation thereof is intended to cover non-exclusive inclusion.

[0026] The utility model will be further described in detail below in combination with the drawings.

[0027] An electronic detonator production waste gas treatment device, as shown in Figure 1 The device comprises:

[0028] The processing tower 1 is made of glass fiber reinforced plastic material with excellent acid and alkali resistance, corrosion resistance, high temperature resistance and high strength, etc. The bottom of the processing tower 1 is provided with an air inlet pipe 3. The air inlet pipe 3 is provided with an electromagnetic air valve 4 at the top. One end of the air inlet pipe 3 is connected with the side wall of the processing tower 1, and the other end is connected with the workshop waste gas collecting pipeline. The top of the processing tower 1 is provided with an air outlet pipe 5. The air outlet pipe 5 is provided with an electromagnetic air valve 4. One end of the air outlet pipe 5 is connected with the processing tower 1, and the other end is connected with the inlet of the terminal negative pressure fan. The air outlet pipe 5 and the air inlet pipe 3 are circular pipes. The bottom of the air outlet pipe 5 and the air inlet pipe 3 is provided with a drain pipe. The drain pipe is provided with a drain valve. The front side of the processing tower 1 is provided with a water tank 2. The rear side wall of the water tank 2 is provided with a water inlet 8. The water inlet 8 is about 30 cm high. The water tank 2 is connected with the inside of the processing tower 1 through the water inlet 8. The top of the water tank 2 is provided with a window 6. The window 6 is provided with a cover 7. The cover 7 is overlapped on the top of the water tank 2. The bottom of the cover 7 is formed with a rib ring which is matched with the window 6. A large number of sensors are arranged on the water tank 2. The sensors measure the liquid level, PH, ORP, conductivity and other parameters of the internal water.

[0029] The displacement structure is shown in Figure 3 . The displacement structure includes a water supplement pipe 10, a drain pipe 9 and a dosing pipe 11. The drain pipe 9 is connected with the bottom of the side wall of the water tank 2. The water supplement pipe 10 and the dosing pipe 11 are arranged on the left and right sides of the water tank 2 respectively. The water supplement pipe 10 and the dosing pipe 11 are connected with the top wall of the water tank 2. The water supplement pipe 10, the drain pipe 9 and the dosing pipe 11 are respectively provided with water valves (the water valves are electromagnetic valves).

[0030] The spraying structure is shown in Figure 4 . The spraying structure includes a water suction pipe 12, a high-pressure water pump 13, a filter 14, a water distribution pipe 15 and a spray head 16. The high-pressure water pump 13 is fixed on the top of the water tank 2. The input end of the high-pressure water pump 13 is connected with the bottom of the water tank 2 through the water suction pipe 12. The water distribution pipe 15 is fixed in the processing tower 1 and is horizontally arranged on the top of the processing tower 1 (the specific shape of the water distribution pipe 15 is shown in Figure 4 . The water distribution pipe 15 is a regular octagonal ring pipe with two communication circles). A plurality of spray heads 16 are uniformly arranged on the water distribution pipe 15. The filter 14 is a Y-shaped filter. One end of the filter 14 is connected with the output end pipe of the high-pressure water pump 13. The other end of the filter 14 is connected with the water distribution pipe 15 through a pipe.

[0031] The high-efficiency reaction layer includes a sieve plate 17 and a molecular sieve. The sieve plate 17 is fixed in the processing tower 1 and is horizontally arranged below the water distribution pipe 15. The molecular sieve is stacked on the sieve plate 17. The molecular sieve has many uniform pore channels and orderly arranged holes in structure. These holes can adsorb molecules smaller than the diameter of the holes into the holes. The molecular sieve has preferential adsorption capacity for polar molecules and unsaturated molecules and has very high specific surface area, which is beneficial to adsorption and catalytic reaction. Figure 5As shown, the spiral flow guide 18 is uniformly provided with eight fan structures in the circumferential direction, and all the fan structures are arranged in the same direction of spiral rising. The spiral flow guide 18 is fixed in the treatment tower 1 and arranged between the sieve plate 17 and the connecting port of the air inlet pipe 3. The exhaust gas forms a cyclone below the spraying structure through the spiral flow guide 18.

[0032] A pressure gauge is installed at a corresponding position on each water pipe, and an air pressure gauge is installed at a corresponding position of the air outlet pipe 5 and the air inlet pipe 3.

[0033] In the specific implementation of the embodiment:

[0034] Before treating the exhaust gas, the water supplement pipe 10 is opened to start adding water into the treatment tower 1. When the water level exceeds the water inlet port 8 by about 25 cm, the high-pressure water pump 13 is opened to start spraying, and the molecular sieve is wetted. When the water level is about 60-65 cm, the water supplement is stopped, the chemical adding pipe 11 is opened to add treatment chemicals into the water body (the first addition needs to be over-added), and the addition is stopped after enough chemicals are added. After 10-20 minutes, the treatment chemicals and water are fully mixed in the spraying and falling circulation.

[0035] The exhaust gas treatment is started. The air valves 4 of the air outlet pipe 5 and the air inlet pipe 3 are opened, and the end negative pressure fan is started. Part of the exhaust gas (acid and alkali exhaust gas, nitrogen-containing exhaust gas, and fluorine-containing exhaust gas) generated in the workshop is absorbed and collected, and is sent into the treatment tower 1 through the air inlet pipe 3. After passing through the spiral flow guide 18, the exhaust gas is guided by the spiral flow guide 18 to form a cyclone, so that the gas in the treatment tower 1 is uniformly mixed, and the wind speed is reduced. The exhaust gas enters the high-efficiency reaction layer in the form of a cyclone, contacts the liquid remaining on the molecular sieve in the molecular sieve pile, and the gas passes through the high-efficiency reaction layer and contacts the chemical dilution liquid sprayed and fallen from above, so that the harmful components in the exhaust gas are reacted and dissolved in the liquid. The treated exhaust gas falls to the bottom of the treatment tower 1 (the molecular sieve layer and the spraying structure increase the contact effect of the exhaust gas and the treatment liquid, improve the exhaust gas treatment capacity, and the exhaust gas reacts with the treatment liquid flowing on the fan structure of the spiral flow guide 18 during the rising process), and is discharged from the treatment tower 1 through the air outlet pipe 5 and is sent into the chimney by the negative pressure fan for standard high-altitude emission.

[0036] During the treatment of the exhaust gas, the water level, PH, ORP, and conductivity of the water body in the treatment tower 1 are monitored, and the water is replaced and chemicals are added according to the parameters. When the water is replaced, the water level is not less than 20 cm.

[0037] The above has described the utility model and its implementation mode, which is not restrictive, and the drawings only show one of the implementation modes of the utility model, and the actual structure is not limited thereto. In summary, if a person skilled in the art is inspired thereby, without departing from the creative purpose of the utility model, similar structural modes and embodiments are not creatively designed, which should belong to the protection scope of the utility model.

Claims

1. An exhaust gas treatment device for electronic detonator production, characterized by, The utility model relates to a high -efficient waste gas treatment device, including: processing tower (1), bottom connection has air inlet pipe (3), top connection has air outlet pipe (5), and air inlet pipe (3) and air outlet pipe (5) are provided with air valve (4) respectively, waste gas enters processing tower (1) through air inlet pipe (3), and leaves after processing through air outlet pipe (5); Water tank (2) and replacement structure; water tank (2) is arranged in the front side of processing tower (1), and the replacement structure is arranged on the water tank (2), and the water tank (2) is replaced by the replacement structure to the water body in processing tower (1); Spraying structure, arranged in the top of processing tower (1); High -efficient reaction layer, arranged below the spraying structure, and the exhaust gas is contacted with water body in high -efficient reaction layer; Screw cover spiral flow guide piece (18) is arranged below the high -efficient reaction layer, and the exhaust gas forms cyclone through spiral flow guide piece (18).

2. The electronic detonator production exhaust gas treatment device according to claim 1, characterized in that: The rear wall bottom of water tank (2) is reserved with water passage (8), and is communicated with the inside of processing tower (1) through water passage (8), and the top of water tank (2) is reserved with window (6), and window (6) is equipped with cover (7).

3. The electronic detonator production exhaust treatment device according to claim 2, characterized in that: The replacement structure includes water replenishing pipe (10), drain pipe (9) and dosing pipe (11); the drain pipe (9) is connected with the bottom of the side wall of the water tank (2), the water replenishing pipe (10) and the dosing pipe (11) are arranged on the left and right sides of the water tank (2) respectively and connected with the top wall of the water tank (2), and the water replenishing pipe (10), the drain pipe (9) and the dosing pipe (11) are respectively provided with water valves.

4. The electronic detonator production exhaust treatment device according to claim 1, characterized in that: The spraying structure includes water pumping pipe (12), high-pressure water pump (13), filter (14), water distribution pipe (15) and spray head (16); the high-pressure water pump (13) is fixed on the top of the water tank (2), the input end of the high-pressure water pump is connected with the bottom of the water tank (2) through the water pumping pipe (12), the water distribution pipe (15) is fixed in the processing tower (1) and horizontally arranged on the top of the processing tower (1), a plurality of spray heads (16) are uniformly arranged on the water distribution pipe (15), the filter (14) is a Y-shaped filter, one end of which is connected with the output pipeline of the high-pressure water pump, and the other end is connected with the water distribution pipe (15) through a pipeline.

5. The electronic detonator production exhaust treatment device according to claim 4, characterized in that: The high -efficient reaction layer includes sieve plate (17) and molecular sieve;Sieve plate (17) is fixed in processing tower (1), and is horizontally arranged below water distribution pipe (15), and molecular sieve is placed on sieve plate (17).

6. The electronic detonator production exhaust treatment device according to claim 5, characterized in that: The spiral flow guide piece (18) is uniformly provided with a plurality of fan blade structures along the circumference, and the fan blade structures are arranged in a spiral upward manner, the spiral flow guide piece (18) is fixed in the processing tower (1) and arranged above the air inlet pipe (3).