Desulfurizing tower with observation hole

Abstract

The utility model relates to the technical field of environmental protection equipment, in particular to a desulfurizing tower with an observation hole, which comprises a tower body, the tower body is composed of a plurality of sections of barrels, a high-pressure flushing system is arranged in the tower body, an air inlet is arranged on the side surface of the bottom of the tower body, a sieve plate is arranged at the lower part in the tower body, and the observation hole is formed in the sieve plate. A ridge type tray is arranged above the sieve plate, a spraying layer is arranged above the ridge type tray, a spiral atomizing nozzle is arranged on the spraying layer, a demister is arranged above the spraying layer, an exhaust port is formed in the position, located at the top end in the tower body, above the demister, and an observation hole is formed in the lower portion of the demister. A quick-open sealing cover is arranged on the observation hole, and a sensor module is arranged below the observation hole. According to the utility model, the observation hole and the sensor module are additionally arranged, and the tower body is subjected to sectional design for blocking prevention, mass transfer structure optimization and the like, so that the problems of desulfurization efficiency, scaling and blockage in the tower are monitored in real time.

Description

Technical Field

[0001] This utility model relates to the field of environmental protection equipment technology, specifically a desulfurization tower with an observation hole. Background Technology

[0002] Desulfurization towers are important equipment for removing harmful gases such as sulfur dioxide from flue gas. Traditional desulfurization towers have the following three technical defects during operation: (1) Difficulty in monitoring scaling and clogging: Areas such as the packing layer and spray layer inside the tower are prone to scaling due to sulfide deposition or slurry crystallization, which leads to a decrease in mass transfer efficiency or even clogging. Traditional desulfurization towers lack direct monitoring methods and require manual inspection after shutdown, which affects production efficiency; (2) Unstable desulfurization efficiency: Parameters such as desulfurization liquid circulation volume and sulfur capacity are difficult to adjust dynamically, resulting in fluctuations in desulfurization efficiency; (3) High maintenance costs: Traditional cleaning processes require frequent shutdowns and the use of robots or high-pressure cleaning equipment, which are complex to operate and costly.

[0003] While some existing desulfurization towers are equipped with sensors or monitoring devices, these devices are costly and prone to failure in certain harsh environments. Therefore, how to install a simple and practical observation device on the desulfurization tower has become an urgent problem for those skilled in the art. Utility Model Content

[0004] In view of the shortcomings of the existing technology, the purpose of this utility model is to provide a desulfurization tower with an observation hole to solve the problems mentioned in the background art.

[0005] To achieve the above objectives, the present invention adopts the following technical solution: The present invention provides a desulfurization tower with an observation hole, comprising a tower body composed of several cylindrical sections. A high-pressure flushing system is installed inside the tower body. An air inlet is provided on the bottom side surface of the tower body. A sieve plate is installed at the lower part of the tower body. A ridge-type tray is installed above the sieve plate. A spray layer is installed above the ridge-type tray. The spray layer is equipped with spiral atomizing nozzles. A demister is installed above the spray layer. An exhaust port is installed above the demister at the top of the tower body. An observation hole is installed below the demister. A quick-opening sealing cover is installed on the observation hole. A sensor module is installed below the observation hole.

[0006] Preferably, the tower body is a segmented design with a total height of 45 meters, consisting of 30 sections, each section being 1.5 meters long, and the joints of the sections are sealed with acid-resistant mortar.

[0007] Preferably, the inner layer of the tower is a granite anti-corrosion layer, and the outer layer is a carbon steel layer.

[0008] Preferably, the ridge-type tray is a perforated tray with an inclination angle of 15°, a hole diameter of 50 mm, and is made of 316L stainless steel.

[0009] Preferably, the spray layer is configured as four layers, with a spacing of 4 meters between each layer.

[0010] Preferably, the spiral atomizing nozzle is configured with a double spiral structure, the nozzle diameter is 12-30 mm, and it is made of 316L stainless steel.

[0011] Preferably, the tower body is provided with a number of observation holes, which are located in the spray layer area, the sieve plate area and below the demister.

[0012] Preferably, the observation hole is provided with a viewing window inside, the viewing window is located inside the quick-opening sealing cover, the diameter of the viewing window is 150-300 mm, and the viewing window is made of double-layer tempered glass or polycarbonate material.

[0013] Preferably, the sensor module includes a pH meter, a turbidity sensor, and a high-definition camera.

[0014] Preferably, the demister includes swirl blades and a shroud.

[0015] Compared with the prior art, the advantages and positive effects of this utility model are as follows:

[0016] This utility model provides a desulfurization tower with an observation port. By adding an observation port and sensor module, including segmented tower design for anti-clogging and optimized mass transfer structure, it enables real-time monitoring of desulfurization efficiency, scaling, and clogging issues within the tower. Through structural optimization and the installation of detection devices, operators can directly observe the desulfurization reaction within the tower, achieving visualization and dynamic control of the tower's operating conditions. Overall, this utility model has the following advantages: 1. Real-time monitoring and early warning: Through the observation port and sensors, desulfurization efficiency and scaling levels can be dynamically monitored, reducing unplanned downtime. 2. Improved anti-clogging performance: The ridge-type tray and large-diameter nozzle design reduce the risk of tower clogging, increasing sulfur capacity by 50%. 3. Convenient maintenance: The quick-opening observation port supports rapid cleaning or component replacement, reducing maintenance costs by more than 30%. 4. Compact and efficient structure: The tower height is reduced by 1 / 3 compared to traditional packed towers, reducing the floor space required and making it suitable for industrial scenarios with limited space. Attached Figure Description

[0017] To more clearly illustrate the technical solutions of the embodiments of this utility model, the drawings used in the description of the embodiments will be briefly introduced below. Obviously, the drawings described below are some embodiments of this utility model. For those skilled in the art, other drawings can be obtained based on these drawings without creative effort.

[0018] Figure 1 This is a schematic diagram of the overall structure of this utility model.

[0019] In the diagram, 1. Tower body; 2. Observation hole; 3. Spray layer; 4. Ridge tray; 5. Demister; 6. Spiral atomizing nozzle; 7. Sensor module; 8. Quick-opening sealing cover; 9. Air inlet; 10. Exhaust outlet; 11. Screen plate; 12. High-pressure flushing system; 13. Cover; 14. Swirl blades; 15. Viewing window. Detailed Implementation

[0020] To better understand the above-mentioned objectives, features, and advantages of this utility model, the present utility model will be further described below with reference to the accompanying drawings and embodiments. It should be noted that, unless otherwise specified, the embodiments and features described in these embodiments can be combined with each other.

[0021] Many specific details are set forth in the following description in order to provide a full understanding of the present invention. However, the present invention may also be implemented in other ways different from those described herein. Therefore, the present invention is not limited to the specific embodiments disclosed in the following specification.

[0022] The attached figure shows a specific embodiment of this utility model. This embodiment aims to provide a desulfurization tower with an observation port, including a tower body 1, for carrying out the overall desulfurization process. The tower body 1 is composed of several cylindrical sections, which facilitates segmented disassembly and maintenance. A high-pressure flushing system 12 is installed inside the tower body 1, and a sensor module 7 monitors the liquid film thickness in real time. If the scale exceeds 2 mm... If the threshold value is reached (mm), the high-pressure flushing system 12 is activated to flush the tower body 1. An air inlet 9 is provided on the bottom side surface of the tower body 1 to receive flue gas. A sieve plate 11 is provided inside the lower part of the tower body 1 to perform preliminary screening of the flue gas, leaving large particles. A ridge-type tray 4 is provided above the sieve plate 11. The ridge-type tray 4 reduces the risk of tower blockage and increases sulfur capacity. A spray layer 3 is provided above the ridge-type tray 4. After passing through the ridge-type tray 4 and the spray layer 3, the flue gas comes into countercurrent contact with the spray liquid, completing preliminary desulfurization. The spray layer 3 is equipped with spiral atomizing nozzles 6. The spray liquid forms uniform droplets through the spiral atomizing nozzles 6, further absorbing sulfur dioxide in the flue gas. The large-diameter nozzle design also reduces the risk of tower blockage. A demister 5 is provided above the spray layer 3, using a combination structure of swirl blades 14 and a shroud 13. After being purified by the liquid droplets, the flue gas is dehydrated by the demister 5 and discharged in compliance with standards. An exhaust port 10 is set at the top of the tower body 1 above the demister 5. The qualified flue gas is discharged from the exhaust port 10. An observation hole 2 is set below the demister 5. Observation holes 2 are set in areas prone to scaling, such as between spray layers 3, in the sieve plate 11 area, and below the demister 5. Through structural optimization and the setting of observation holes 2 and sensor module 7, it is convenient for operators to directly observe the desulfurization reaction in the tower body 1, realize the visualization and dynamic control of the working conditions in the tower body 1. A quick-opening sealing cover 8 is set on the observation hole 2. The quick-opening sealing cover 8 supports the insertion of detection probes or visual inspection without stopping the machine. A sensor module 7 is set below the observation hole 2. The sensor module 7 integrates an online pH meter, a turbidity sensor and a camera to monitor the liquid film thickness and sulfur particle deposition in real time.

[0023] To better optimize the structure and facilitate segmented disassembly and maintenance, tower body 1 is designed as a segmented structure with a total height of 45 meters, consisting of 30 sections, each 1.5 meters long, with acid-resistant mortar used to seal the joints between the sections.

[0024] To make the structure more compact and efficient, the inner layer of tower body 1 is made of granite anti-corrosion layer, and the outer layer is made of carbon steel layer.

[0025] To improve anti-clogging capabilities, the ridge-type tray 4 is designed as a perforated tray with a 15° tilt angle and 50 mm hole diameter, and is made of 316L stainless steel.

[0026] To enhance the desulfurization effect, spray layer 3 is set to four layers, with a spacing of 4 meters between each layer.

[0027] To enhance the reaction between flue gas and spray liquid for desulfurization, the spiral atomizing nozzle 6 is designed with a double spiral structure, with a nozzle diameter of 12-30 mm, and is made of 316L stainless steel.

[0028] To enhance the observation of areas prone to scaling, several observation holes 2 are provided on the tower body 1. The observation holes 2 are located in areas that are prone to scaling, such as the spray layer 3 area, the sieve plate 11 area, and the demister 5.

[0029] To facilitate observation and increase durability, a viewing window 15 is provided inside the observation hole 2. The viewing window 15 is located inside the quick-opening sealing cover 8. The diameter of the viewing window 15 is 150-300 mm. The viewing window 15 is made of double-layer tempered glass or polycarbonate material.

[0030] To improve detection results, sensor module 7 includes a pH meter, a turbidity sensor, and a high-definition camera.

[0031] To improve the dehydration effect, the demister 5 includes swirl vanes 14 and a cover 13.

[0032] The usage process and working principle of this utility model are as follows: Flue gas enters the bottom of the tower body 1 through the air inlet 9, first passes through the sieve plate 11 to remove large particles, and then passes through the ridge tray 4 and the spray layer 3, where it comes into counter-current contact with the spray liquid from bottom to top to complete the desulfurization process. After that, the purified flue gas is dehydrated by the demister 5 and discharged from the exhaust port 10. This process can be observed in real time through the observation hole 2, and the sensor module 7 is also detecting it in real time. Furthermore, when the sensor module 7 is monitoring the liquid film thickness in real time, if scaling exceeds the 2 mm threshold, the high-pressure flushing system 12 can be activated to flush the inside of the tower body 1.

[0033] The above description is merely a preferred embodiment of the present utility model and is not intended to limit the present utility model in any other way. Any person skilled in the art may make changes or modifications to the above-disclosed technical content to create equivalent embodiments for application in other fields. However, any simple modifications, equivalent changes, and modifications made to the above embodiments based on the technical essence of the present utility model without departing from the technical solution of the present utility model shall still fall within the protection scope of the technical solution of the present utility model.

Claims

1. A desulfurization tower with an observation port, comprising a tower body (1), characterized in that: The tower body (1) is composed of several cylindrical sections. A high-pressure flushing system (12) is installed inside the tower body (1). An air inlet (9) is provided on the bottom side surface of the tower body (1). A sieve plate (11) is provided at the bottom inside the tower body (1). A ridge tray (4) is provided above the sieve plate (11). A spray layer (3) is provided above the ridge tray (4). A spiral atomizing nozzle (6) is provided on the spray layer (3). A demister (5) is provided above the spray layer (3). An exhaust port (10) is provided above the demister (5) at the top inside the tower body (1). An observation hole (2) is provided below the demister (5). A quick-opening sealing cover (8) is provided on the observation hole (2). A sensor module (7) is provided below the observation hole (2).

2. The desulfurization tower with an observation hole according to claim 1, characterized in that: The tower body (1) is a segmented design with a total height of 45 meters. It consists of 30 sections of cylindrical body, each section being 1.5 meters long. The joints of the cylindrical body are sealed with acid-resistant mortar.

3. The desulfurization tower with an observation hole according to claim 1, characterized in that: The inner layer of the tower body (1) is a granite anti-corrosion layer, and the outer layer is a carbon steel layer.

4. The desulfurization tower with an observation hole according to claim 1, characterized in that: The ridge-type tray (4) is a perforated tray with an inclination angle of 15° and a hole diameter of 50 mm. It is made of 316L stainless steel.

5. The desulfurization tower with an observation hole according to claim 1, characterized in that: The spray layer (3) is set to four layers, with a spacing of 4 meters between each layer.

6. The desulfurization tower with an observation hole according to claim 1, characterized in that: The spiral atomizing nozzle (6) is configured with a double spiral structure, with a nozzle diameter of 12-30 mm, and is made of 316L stainless steel.

7. The desulfurization tower with an observation hole according to claim 1, characterized in that: The tower body (1) is provided with several observation holes (2), which are located in the spray layer (3) area, the sieve plate (11) area and below the demister (5).

8. The desulfurization tower with an observation hole according to claim 1, characterized in that: The observation hole (2) is provided with a viewing window (15), which is located inside the quick-opening sealing cover (8). The diameter of the viewing window (15) is 150-300 mm, and the viewing window (15) is made of double-layer tempered glass or polycarbonate material.

9. The desulfurization tower with an observation hole according to claim 1, characterized in that: The sensor module (7) includes a pH meter, a turbidity sensor and a high-definition camera.

10. The desulfurization tower with an observation hole according to claim 1, characterized in that: The demister (5) includes swirl vanes (14) and a cover (13).

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