A gas purification spray tower

By using horizontally distributed purification cylinders and a simplified structural design, the problem of large height and volume of traditional spray towers has been solved, achieving low-cost and high-efficiency gas purification, suitable for various locations.

CN224358189UActive Publication Date: 2026-06-16TAIZHOU LVYE ENVIRONMENTAL PROTECTION ENG CO LTD

Patent Information

Authority / Receiving Office
CN · China
Patent Type
Utility models(China)
Current Assignee / Owner
TAIZHOU LVYE ENVIRONMENTAL PROTECTION ENG CO LTD
Filing Date
2025-06-13
Publication Date
2026-06-16

AI Technical Summary

Technical Problem

Traditional spray tower designs require significant height and volume, resulting in high construction costs, high energy consumption, and difficulty in being applied to spaces with limited space.

Method used

Multiple horizontally distributed purification cylinders, combined with an air intake device and a spray device, simplify the structure, utilize demister balls to further treat the gas, realize the recycling of the purification liquid, and reduce the requirements for height and volume.

🎯Benefits of technology

It reduces construction and operating costs, decreases energy consumption, is suitable for spaces with limited space, and improves purification efficiency and resource utilization.

✦ Generated by Eureka AI based on patent content.

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Patent Text Reader

Abstract

The application relates to the field of gas purification, in particular to a gas purification spray tower which comprises a main body, a plurality of purification cylinders distributed in the main body in a horizontal direction, an air inlet device for conveying gas into the purification cylinders, a spraying device for spraying purification liquid into the purification cylinders, a demisting ball located in the main body and above all the purification cylinders, and a liquid storage pool located below the purification cylinders, wherein the spraying device sucks the purification liquid in the liquid storage pool through a pump body, sprays the purification liquid into the purification cylinders through pipelines and nozzles, and the air inlet device is composed of a main pipeline and a plurality of branch pipelines which are communicated with the lower parts of the purification cylinders. The application has the technical effects of improving the gas purification efficiency, effectively removing mist and recycling the purification liquid.
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Description

Technical Field

[0001] This application relates to the field of gas purification, and in particular to a gas purification spray tower. Background Technology

[0002] In industrial production and environmental protection, gas purification technology is crucial. With the acceleration of industrialization, emissions of various waste gases are increasing daily, posing a serious threat to the environment and human health. Effective gas purification technology can reduce the emission of harmful gases, improve air quality, protect the ecological environment, and also help enterprises meet environmental regulations and achieve sustainable development. Gas purification equipment is constantly being upgraded to adapt to the treatment needs of different industries and different types of waste gases.

[0003] In traditional gas purification methods, spray towers are commonly used equipment. Traditional spray towers are typically designed with a multi-layered structure. When gas enters the tower, it needs to be sprayed through each layer multiple times by water jets to purify the gas. This multi-layered design requires the spray tower to have a considerable height and volume to accommodate the various spray layers and the gas flow space. Furthermore, to ensure effective spraying, it also requires large water pumps and complex piping systems.

[0004] However, this design of traditional spray towers has significant shortcomings. Due to their high requirements for height and volume, construction costs increase substantially, including site occupancy costs, building material costs, and equipment installation costs. Furthermore, their large size and complex structure lead to higher energy consumption during operation and increased maintenance difficulty. Moreover, traditional spray towers are unsuitable for locations with limited space. Utility Model Content

[0005] In order to reduce the operating cost of spray towers, this application provides a gas purification spray tower.

[0006] The gas purification spray tower provided in this application adopts the following technical solution:

[0007] A gas purification spray tower includes a main body, a purification cylinder, an air inlet device, and a spray device.

[0008] The purification cylinders are provided in multiple locations, all of which are located within the main body, with at least two purification cylinders distributed horizontally.

[0009] The air intake device is used to deliver gas into the purification cylinder.

[0010] The spraying device is used to spray purification liquid into the purification cylinder.

[0011] By adopting the above technical solution and setting up multiple horizontally distributed purification cylinders, the design of multi-layer structures is avoided, reducing the requirements for the height and volume of the spray tower, thereby reducing the cost of gas purification. Simultaneously, gas can be supplied to the purification cylinders through the air inlet device, and purification liquid can be sprayed into the purification cylinders using the spray device to achieve gas purification.

[0012] Preferably, it also includes defogging balls.

[0013] The demisting ball is located inside the main body and above all the purification cylinders.

[0014] The exhaust port of the main body is located above the defogging ball.

[0015] By adopting the above technical solution, the demisting balls located above all the purification cylinders are used to further treat the impurities such as mist in the gas, and finally the gas is discharged through the main exhaust port located above the demisting balls, thus achieving gas purification.

[0016] Preferably, it also includes a liquid storage tank.

[0017] The liquid storage tank is located below the purification cylinder.

[0018] The spraying device is also used to pump out the purified liquid in the storage tank.

[0019] By adopting the above technical solution, the spraying device sprays the purification liquid into the purification cylinder, and the purification liquid automatically flows into the storage tank below, realizing the recycling of the purification liquid.

[0020] Preferably, the spraying device includes a pump body, pipelines, and spray nozzles.

[0021] The pump body is used to draw purified liquid from the storage tank.

[0022] The pipeline is connected to the liquid outlet of the pump body.

[0023] The nozzle is provided in multiple parts and is connected to the pipeline. The nozzle is used to spray the purification liquid into the purification cylinder.

[0024] By adopting the above technical solution, the pump body draws the purified liquid from the storage tank and transports it through pipelines to multiple nozzles. The nozzles then spray the purified liquid into the purification cylinder, thereby achieving the purification of the gas in the purification cylinder and the recycling of the purified liquid.

[0025] Preferably, all the purified liquid sprayed from the nozzle flows into the purification cylinder.

[0026] By adopting the above technical solution, it is ensured that the purification liquid fully acts on the gas inside the purification cylinder, thereby improving the purification efficiency.

[0027] Preferably, the nozzle of the spray head is located inside the purification cylinder.

[0028] By adopting the above technical solution, it is ensured that all the sprayed purification liquid flows into the purification cylinder, effectively purifying the gas inside the purification cylinder.

[0029] Preferably, the air intake device includes a main pipe and branch pipes.

[0030] The branch pipe is provided in multiple parts, one end of the branch pipe is connected to the main pipe, and the other end of the branch pipe is connected to the purification cylinder.

[0031] By adopting the above technical solution, the gas can be distributed to various branch pipes through the main pipe and then enter different purification cylinders, realizing simultaneous gas intake and purification of multiple purification cylinders. This avoids the traditional method of using multi-layer spray towers that require spray purification layer by layer, reduces the requirements for the height and volume of the spray tower, and thus reduces the purification cost.

[0032] Preferably, the connection between the branch pipe and the purification cylinder is located at the lower part of the purification cylinder.

[0033] By adopting the above technical solution, the gas enters the purification cylinder from the bottom, which facilitates the spraying device to spray the purification liquid into the purification cylinder to purify the gas.

[0034] Preferably, corresponding to one main pipe: there are two branch pipes.

[0035] By adopting the above technical solution, the two branch pipes corresponding to each main pipe simultaneously deliver gas to the purification cylinder, optimizing the gas delivery method, improving the efficiency of gas entering the purification cylinder, and thus improving the overall working efficiency of the gas purification spray tower.

[0036] In summary, this application includes at least one of the following beneficial technical effects:

[0037] 1. The horizontal distribution of multiple purification cylinders replaces the multi-layer design, reducing the dependence on the height and volume of the spray tower and lowering construction costs such as site, materials and equipment installation;

[0038] 2. The simplified structure reduces operating energy consumption and maintenance difficulty;

[0039] 3. It reduces the requirements for site space and can be applied to places with limited site space. Attached Figure Description

[0040] Figure 1 This is a schematic diagram of a gas purification spray tower according to an embodiment of this application.

[0041] Figure 2 This is a schematic diagram of the maximum distance L0 between the nozzle and the purification cylinder.

[0042] Explanation of reference numerals in the attached drawings: 1. Liquid storage tank; 2. Main body; 3. Purification cylinder; 4. Air inlet device; 41. Main pipe; 42. Branch pipe; 5. Spraying device; 51. Pump body; 52. Pipeline; 53. Nozzle; 6. Demisting ball. Detailed Implementation

[0043] The present application will be further described in detail below with reference to the accompanying drawings.

[0044] Reference Figure 1 This application discloses a gas purification spray tower, including a liquid storage tank 1, a main body 2, a purification cylinder 3, an air inlet device 4, and a spray device 5.

[0045] The storage tank 1 is used to store the purification liquid. The main body 2 is located above the storage tank 1. The purification cylinder 3 has a vertical axis and is located inside the main body 2. There are multiple purification cylinders 3, and at least two purification cylinders 3 are distributed in a horizontal direction. Preferably, all purification cylinders 3 are distributed in a horizontal direction.

[0046] The air intake device 4 is used to supply gas into the purification cylinder 3. The spray device 5 is used to draw out the purification liquid in the storage tank 1 and spray the purification liquid into the purification cylinder 3 to purify the gas inside the purification cylinder 3.

[0047] The air intake device 4 includes a main pipe 41 and a branch pipe 42.

[0048] The main pipe 41 is connected to a gas source, which can be a fan, air pump, etc. The gas source is used to transport exhaust gas into the main pipe 41.

[0049] For each main pipe 41, there are two branch pipes 42. One end of the branch pipe 42 is connected to the main pipe 41, and the other end of the branch pipe 42 is connected to the purification cylinder 3. The connection between the branch pipe 42 and the purification cylinder 3 is located at the lower part of the purification cylinder 3.

[0050] Preferably, two adjacent purification cylinders 3 (connected by two branch pipes 42) are connected to the same main pipe 41. In one embodiment: there are two purification cylinders 3, and one main pipe 41. In other embodiments: there are 2N purification cylinders 3, and N main pipes 41; in this case, the N main pipes 41 can be connected to N gas sources respectively, or the N main pipes 41 can be connected to a main pipe, and the main pipe is connected to a gas source.

[0051] The spraying device 5 includes a pump body 51, a pipeline 52, and a nozzle 53.

[0052] The inlet of the pump body 51 is connected to the storage tank 1, and the pump body 51 is used to draw the purified liquid in the storage tank 1.

[0053] Pipeline 52 is connected to the outlet of pump body 51.

[0054] Multiple nozzles 53 are provided and connected to pipe 52. The nozzles 53 are used to spray purification liquid into the purification cylinder 3.

[0055] All the purified liquid sprayed from nozzle 53 flows into the purification cylinder 3. In one embodiment, the nozzle of nozzle 53 is located inside the purification cylinder 3. In other embodiments, refer to... Figure 2 The purified liquid sprayed from the nozzle 53 is in the shape of a cone or a fan. The maximum distance L0 between the nozzle 53 and the purified cylinder 3 is calculated based on the central angle A of the cone or fan and the inner diameter D of the purified cylinder 3. During installation, the actual distance between the nozzle and the purified cylinder 3 is less than the maximum distance L0.

[0056] Reference Figure 1 A gas purification spray tower also includes demisting balls 6. Multiple demisting balls 6 are provided, located inside the main body 2, and positioned above all the purification cylinders 3. The exhaust port of the main body 2 is located above the demisting balls 6.

[0057] In one embodiment: a support net is connected inside the main body 2, and the defogging ball 6 is placed on the support net.

[0058] Small liquid droplets in the gas are separated using a demister bulb 6. Working mechanism.

[0059] Inertial collision effect: When fog-containing gas passes through the spherical layer at a flow rate of 1.5-3.5 m / s, fog droplets with a diameter >20 μm collide with the surface of the spheres due to inertia [collision efficiency η=1-(Stk / (Stk+0.62))^0.4, where Stk is the Stokes number];

[0060] Centrifugal separation mechanism: The unique fan-shaped blade structure of the multifaceted hollow sphere can generate local swirling airflow (centrifugal acceleration of 50-80g), achieving the separation of 5-10μm fine droplets;

[0061] Surface adsorption: The contact angle of the sphere treated with nano-coating is >150°, and the droplet coalescence rate is increased by more than 40%.

[0062] The implementation principle of a gas purification spray tower according to an embodiment of this application is as follows: This gas purification spray tower uses multiple horizontally distributed purification cylinders 3, changing the multi-layer structure design of traditional spray towers, reducing the requirements for height and volume, and lowering construction costs and operating energy consumption. The air inlet device 4 delivers gas to the lower part of the purification cylinder 3, allowing the gas to flow from bottom to top and fully contact the purification liquid sprayed by the spray device 5, thus achieving gas purification. The demisting ball 6 further removes water mist from the purified gas, ensuring the quality of the discharged gas. The liquid storage tank 1 provides purification liquid to the spray device 5 and enables the recycling of the purification liquid, improving resource utilization. The overall structure is compact and functionally complete, effectively solving the problems existing in traditional spray towers, and making a significant improvement and contribution to the prior art.

[0063] The above are all preferred embodiments of this application, and are not intended to limit the scope of protection of this application. Therefore, all equivalent changes made in accordance with the structure, shape and principle of this application should be covered within the scope of protection of this application.

Claims

1. A gas purification spray tower, characterized in that, It includes the main body (2), the purification cylinder (3), the air intake device (4), the spray device (5), and the demisting ball (6). Multiple purification cylinders (3) are provided, all of which are located inside the main body (2), and at least two purification cylinders (3) are distributed in the horizontal direction. The air intake device (4) is used to deliver gas into the purification cylinder (3). The spraying device (5) is used to spray the purifying liquid into the purifying cylinder (3); The defogging ball (6) is located inside the main body (2), and the defogging ball (6) is located above all the purification cylinders (3). The exhaust port of the main body (2) is located above the defogging ball (6).

2. The gas purification spray tower according to claim 1, characterized in that, It also includes a liquid storage tank (1). The storage tank (1) is located below the purification cylinder (3). The spray device (5) is also used to draw the purified liquid in the storage tank (1).

3. A gas purification spray tower according to claim 2, characterized in that, The spraying device (5) includes a pump body (51), a pipeline (52), and a nozzle (53). The pump body (51) is used to draw the purified liquid from the storage tank (1). The pipeline (52) is connected to the outlet of the pump body (51). The nozzle (53) is provided in multiple ways and is connected to the pipeline (52). The nozzle (53) is used to spray the purification liquid into the purification cylinder (3).

4. A gas purification spray tower according to claim 3, characterized in that, All the purified liquid sprayed from the nozzle (53) flows into the purification cylinder (3).

5. A gas purification spray tower according to claim 4, characterized in that, The nozzle (53) is located inside the purification cylinder (3).

6. A gas purification spray tower according to claim 1, characterized in that, The air intake device (4) includes a main pipe (41) and a branch pipe (42). The branch pipe (42) is provided in multiple ways. One end of the branch pipe (42) is connected to the main pipe (41), and the other end of the branch pipe (42) is connected to the purification cylinder (3).

7. A gas purification spray tower according to claim 6, characterized in that, The connection between the branch pipe (42) and the purification cylinder (3) is located at the lower part of the purification cylinder (3).

8. A gas purification spray tower according to claim 7, characterized in that, Corresponding to one main pipe (41): two branch pipes (42) are provided.