A coke oven gas primary cooler spray cleaning device
Patent Information
- Application Number
- CN202522044349.1
- Authority / Receiving Office
- CN · China
- Patent Type
- Utility models(China)
- Current Assignee / Owner
- Filing Date
- 2025-09-23
- Publication Date
- 2026-09-08
- Estimated Expiration
- 2035-09-23
AI Technical Summary
[0002]焦炉煤气中高含量的萘是一个棘手的问题,它不仅会在煤气管道中凝结成片状结晶,导致管线堵塞,还会影响脱硫化氢的效率,进而影响整个煤气净化系统的运行
通过连接管一以及连接管二的设计,方便将其外接供液设备,实现了连接管一以及连接管二分别对喷淋头一以及喷淋头二的供液,在进行喷淋洗萘的过程中,可以根据煤气中萘的含量分别调节两个连接管一以及连接管二内清洗液的浓度,实现了上下两端喷淋液浓度的分开调节,能够根据煤气中杂质的含量和喷淋效果的需求,灵活调整喷淋溶液的浓度,有效保证了装置对煤气的清洗效果。
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Figure CN224728490U_ABST
Abstract
Description
Technical Field
[0001] This utility model relates to the technical field of spray purification devices, specifically to a spray purification device for a coke oven gas primary cooler. Background Technology
[0002] High naphthalene content in coke oven gas is a challenging problem. It not only condenses into flaky crystals in gas pipelines, causing blockages, but also affects the efficiency of hydrogen sulfide removal, thus impacting the operation of the entire gas purification system. In winter, naphthalene in coke oven gas easily condenses into a solid when the temperature drops, especially in the 30-40°C range. When the naphthalene content reaches 900-2100 mg / m³, it is more likely to deposit on the surfaces of pipelines and equipment, and it also affects the conversion performance of hydrogenation catalysts, impairing their conversion efficiency. Existing coke oven gas primary cooler spray purification devices use spray heads to evenly spray tar, allowing the spray liquid to fully contact and clean the naphthalene and tar in the gas. Although the above method can achieve the cleaning effect of the device on naphthalene in the gas, when cleaning, the content of impurities in the gas varies. When using the same concentration of cleaning liquid for spraying, it is easy to have incomplete cleaning or waste of cleaning liquid, resulting in poor gas purification effect of the device. Utility Model Content
[0003] (a) Technical problems to be solved The technical problem to be solved by this utility model is to provide a coke oven gas primary cooler spray purification device that allows for convenient and flexible adjustment of the concentration of the spray solution, in light of the current state of the technology.
[0004] (II) Technical Solution This utility model is achieved through the following technical solution: This utility model proposes a spray purification device for a coke oven gas primary cooler, including a workbench. A spray box is installed on one side of the top of the workbench. Two sets of limiting slide rails are symmetrically arranged at the top of the spray box. A horizontal plate is installed between the upper limiting slide rails. Activated carbon particles are filled in the middle of the horizontal plate. A grid plate is arranged between the lower limiting slide rails. A condensation circulation pipe is connected to the side wall of the grid plate. A connecting pipe is arranged in the middle of the spray box. A spray head is connected to the bottom of the connecting pipe. A second connecting pipe is installed at the bottom of the connecting pipe. A second spray head is arranged at the bottom of the second connecting pipe. A gas supply pipe is arranged on one side wall of the spray box at the bottom of the second connecting pipe. A guide plate is arranged at the bottom of the spray box. A water outlet pipe is installed at the bottom of one side wall of the spray box. A one-way solenoid valve is connected to the water outlet pipe. An exhaust pipe is installed in the middle of the top of the spray box.
[0005] Furthermore, the spray box is connected to the filter box through the air supply pipe. An air inlet pipe is provided on one side wall of the filter box. A dust collection hopper is installed at the bottom of the filter box. Limiting blocks are symmetrically arranged on both sides of the dust collection hopper and on both sides of the top of the filter box. A coarse filter plate is arranged between the limiting blocks at one end, a fine filter plate is installed between the limiting blocks in the middle, and an adsorption plate is arranged between the limiting blocks at the other end.
[0006] Furthermore, the air supply pipe is flange-connected to both the spray box and the filter box, the air inlet pipe is flange-connected to the filter box, and the ash collection hopper is slidably connected to the filter box.
[0007] Furthermore, the limiting block is screwed to the filter box and the ash collection hopper, the coarse filter plate, the fine filter plate and the adsorption plate are slidably connected to the limiting block, and handles are provided at the top of the coarse filter plate, the fine filter plate and the adsorption plate.
[0008] Furthermore, the limiting slide rail is screwed to the spray box, and the horizontal plate and the grid plate are slidably connected to the spray box.
[0009] Furthermore, the activated carbon particles are connected to the horizontal plate slot, the condensation circulation pipe is connected to the horizontal grid slot of the grid plate, and the guide plate is inclined at 60 degrees.
[0010] Furthermore, the water outlet pipe is plugged into the spray box, the one-way solenoid valve is connected to the flange of the water outlet pipe, both the first connecting pipe and the second connecting pipe are plugged into the spray box, the first spray head is plugged into the first connecting pipe, and the second spray head is plugged into the second connecting pipe.
[0011] (III) Beneficial Effects Compared with the prior art, this utility model has the following advantages: The design of connecting pipes one and two facilitates the connection to external liquid supply equipment, enabling connecting pipes one and two to supply liquid to spray head one and spray head two respectively. During the spray washing of naphthalene, the concentration of the cleaning liquid in connecting pipes one and two can be adjusted according to the naphthalene content in the coal gas, realizing separate adjustment of the spray liquid concentration at both ends. The concentration of the spray solution can be flexibly adjusted according to the impurity content in the coal gas and the requirements of the spraying effect, effectively ensuring the cleaning effect of the device on the coal gas. Attached Figure Description
[0012] Figure 1 This is a schematic diagram of the structure of a coke oven gas primary cooler spray purification device according to the present invention; Figure 2This is a front sectional view of the spray box in the spray purification device for a coke oven gas primary cooler described in this utility model; Figure 3 This is a front sectional view of the filter box in the spray purification device for a coke oven gas primary cooler described in this utility model.
[0013] The annotations in the attached figures are explained as follows: 1. Spray box; 2. Handle; 3. Filter box; 4. Workbench; 5. Exhaust pipe; 6. Activated carbon granules; 7. Limiting slide rail; 8. Horizontal plate; 9. Condensation circulation pipe; 10. Connecting pipe one; 11. Spray head two; 12. Guide plate; 13. Grating plate; 14. Spray head one; 15. Connecting pipe two; 16. Water outlet pipe; 17. One-way solenoid valve; 18. Fine filter plate; 19. Air supply pipe; 20. Adsorption plate; 21. Coarse filter plate; 22. Ash collection hopper; 23. Limiting block; 24. Air inlet pipe. Detailed Implementation
[0014] To make the objectives, technical solutions, and advantages of this utility model clearer, the present utility model will be further described in detail below with reference to the accompanying drawings and embodiments. It should be understood that the specific embodiments described herein are merely illustrative of the present utility model and are not intended to limit the present utility model.
[0015] like Figures 1-3As shown, a coke oven gas primary cooler spray purification device in this embodiment includes a workbench 4. A spray box 1 is installed on one side of the top of the workbench 4. Two sets of limiting slide rails 7 are symmetrically arranged at the top of the spray box 1. A horizontal plate 8 is installed between the upper limiting slide rails 7. Activated carbon particles 6 are filled in the middle of the horizontal plate 8. A grid plate 13 is arranged between the lower limiting slide rails 7. A condensation circulation pipe 9 is connected to the side wall of the grid plate 13. A connecting pipe 10 is arranged in the middle of the spray box 1. A spray head 14 is connected to the bottom of the connecting pipe 10. A connecting pipe 2 15 is installed at the lower end of the connecting pipe 10. A spray head 2 11 is arranged at the bottom of the connecting pipe 2 15. The connecting pipes 10 and 2 15 are arranged in rows, with no less than two rows, so that the spray range of the spray head 14 and the spray head 2 11 can cover the entire spray surface. The design of the first pipe 10 and the second pipe 15 facilitates the connection to an external liquid supply device, enabling the first pipe 10 and the second pipe 15 to supply liquid to the first spray head 14 and the second spray head 11 respectively. During the spray washing of naphthalene, the concentration of the cleaning liquid in the two connecting pipes 10 and the second pipe 15 can be adjusted according to the naphthalene content in the gas, realizing the separate adjustment of the concentration of the spray liquid at the upper and lower ends. The concentration of the spray solution can be flexibly adjusted according to the content of impurities in the gas and the requirements of the spraying effect, effectively ensuring the cleaning effect of the device on the gas. A gas supply pipe 19 is set on one side wall of the spray box 1 at the bottom of the second pipe 15. A guide plate 12 is arranged at the bottom of the spray box 1. A water outlet pipe 16 is installed at the bottom of one side wall of the spray box 1. A one-way solenoid valve 17 is connected in the water outlet pipe 16. An exhaust pipe 5 is installed at the middle of the top of the spray box 1.
[0016] like Figures 1-3 As shown, in this embodiment, the spray box 1 is connected to the filter box 3 through the air supply pipe 19. An air inlet pipe 24 is provided on one side wall of the filter box 3. A dust collection hopper 22 is installed at the bottom of the filter box 3. Limiting blocks 23 are symmetrically arranged on both sides of the dust collection hopper 22 and on both sides of the top of the filter box 3. A coarse filter plate 21 is arranged between the limiting blocks 23 at one end. A fine filter plate 18 is installed between the limiting blocks 23 in the middle. An adsorption plate 20 is arranged between the limiting blocks 23 at the other end.
[0017] like Figures 1-3 As shown, in this embodiment, the gas supply pipe 19 is flange-connected to both the spray box 1 and the filter box 3, the air inlet pipe 24 is flange-connected to the filter box 3, and the ash collection hopper 22 is slidably connected to the filter box 3. The ash collection hopper 22 facilitates the collection of falling dust particles, and the air inlet pipe 24 enables the transportation of coke oven gas.
[0018] like Figures 1-3As shown, in this embodiment, the limiting block 23 is screwed to the filter box 3 and the ash collection hopper 22. The coarse filter plate 21, the fine filter plate 18 and the adsorption plate 20 are slidably connected to the limiting block 23. The top of the coarse filter plate 21, the fine filter plate 18 and the adsorption plate 20 are all provided with handles 2. The coarse filter plate 21, the fine filter plate 18 and the adsorption plate 20 realize the pre-filtration of the coal gas, which can prevent impurities in the coal gas from directly entering the spray box 1 and damaging the working equipment inside the spray box 1. The design of the limiting block 23 makes it convenient to remove and replace the three at any time, ensuring the filtration effect of the device on the coal gas.
[0019] like Figures 1-3 As shown, in this embodiment, the limiting slide rail 7 is screwed to the spray box 1, and the horizontal plate 8 and the grid plate 13 are slidably connected to the spray box 1. The design of the limiting slide rail 7 makes it convenient to pull out the horizontal plate 8 or the grid plate 13 for maintenance.
[0020] like Figures 1-3 As shown, in this embodiment, activated carbon particles 6 are connected to the horizontal plate 8 via a slot, condensation circulation pipe 9 is connected to the horizontal grid slot of the grid plate 13, and the guide plate 12 is inclined at 60 degrees. Activated carbon particles 6 can adsorb and discharge odors in the coal gas, effectively ensuring the cleanliness of the coal gas in the discharge device. Condensation circulation pipe 9 can exchange and discharge heat in the coal gas.
[0021] like Figures 1-3 As shown, in this embodiment, the water outlet pipe 16 is plugged into the spray box 1, the one-way solenoid valve 17 is flange-connected to the water outlet pipe 16, the connecting pipe 10 and the connecting pipe 2 15 are both plugged into the spray box 1, the spray head 14 is plugged into the connecting pipe 10, and the spray head 2 11 is plugged into the connecting pipe 2 15. The design of the water outlet pipe 16 in conjunction with the one-way solenoid valve 17 facilitates the one-way discharge of the used spray liquid, so that the discharged spray liquid can be centrally processed. The connecting pipe 10 supplies liquid to the spray head 14, and the connecting pipe 2 15 supplies liquid to the spray head 2 11. There are no less than two rows of spray heads 14 and spray heads 2 11.
[0022] The specific implementation process of this embodiment is as follows: When using the device, the workbench 4 of the device needs to be installed in an appropriate position, and the device needs to be connected to an external power source. The air inlet pipe 24 of the device is connected to the gas supply equipment for coke oven gas. After the gas enters the filter box 3, the coarse filter plate 21 and the fine filter plate 18 can filter the impurity particles in the gas. Combined with the adsorption plate 20 adsorbing the gas, it can effectively prevent impurities in the gas from entering the spray box 1. Then, the connecting pipe 10 and the connecting pipe 25 are connected to the liquid supply equipment respectively, realizing the delivery of spray to the connecting pipe 10 and the connecting pipe 25 respectively. During the transportation process, the concentration of the spray liquid can be adjusted sequentially according to the actual naphthalene content in the coal gas, so that the spray head 14 and spray head 11 can spray the coal gas evenly, realizing the reaction and dissolution between naphthalene in the coal gas and the spray liquid. Then, when the coal gas passes through the grid plate 13, the condensation circulation pipe 9 on the grid in the middle of the grid plate 13 will adsorb and exchange the heat in the coal gas, realizing the cooling of the coal gas by the device. Combined with the secondary adsorption of activated carbon particles 6, the purity of the discharged coal gas is effectively guaranteed. After the spray liquid flows out of the water outlet pipe 16 through the guide plate 12, it is convenient for centralized treatment.
[0023] The above description of the disclosed embodiments enables those skilled in the art to make or use the present invention. Various modifications to these embodiments will be readily apparent to those skilled in the art, and the general principles defined herein may be implemented in other embodiments without departing from the spirit or scope of the present invention. Therefore, the present invention is not to be limited to the embodiments shown herein, but is to be accorded the widest scope consistent with the principles and novel features disclosed herein.
Claims
1. A spray purification device for a primary cooler of coke oven gas, characterized in that: The system includes a workbench (4), on one side of the top of the workbench (4) a spray box (1), two sets of limiting slide rails (7) are symmetrically arranged at the top of the spray box (1), a horizontal plate (8) is installed between the upper limiting slide rails (7), the middle of the horizontal plate (8) is filled with activated carbon particles (6), and a grid plate (13) is arranged between the lower limiting slide rails (7). A condensation circulation pipe (9) is connected to the inner side wall of the grid plate (13), and a connecting pipe (10) is arranged in the middle of the spray box (1). The bottom end of the connecting pipe (10) is connected to... A first spray head (14) is connected to the first connecting pipe (10). A second connecting pipe (15) is installed at the lower end of the first connecting pipe (10). A second spray head (11) is arranged at the bottom end of the second connecting pipe (15). An air supply pipe (19) is arranged on one side wall of the spray box (1) at the bottom end of the second connecting pipe (15). A guide plate (12) is arranged at the bottom end of the spray box (1). A water outlet pipe (16) is installed at the bottom end of one side wall of the spray box (1). A one-way solenoid valve (17) is connected inside the water outlet pipe (16). An exhaust pipe (5) is installed at the middle of the top of the spray box (1).
2. The coke oven gas primary cooler spray purification device according to claim 1, characterized in that: The spray box (1) is connected to the filter box (3) through the air supply pipe (19). An air inlet pipe (24) is provided on one side wall of the filter box (3). A dust collection hopper (22) is installed at the bottom of the filter box (3). Limiting blocks (23) are symmetrically arranged on both sides of the dust collection hopper (22) and on both sides of the top of the filter box (3). A coarse filter plate (21) is arranged between the limiting blocks (23) at one end. A fine filter plate (18) is installed between the limiting blocks (23) in the middle. An adsorption plate (20) is arranged between the limiting blocks (23) at the other end.
3. The coke oven gas primary cooler spray purification device according to claim 2, characterized in that: The gas supply pipe (19) is flange-connected to the spray box (1) and the filter box (3), the air inlet pipe (24) is flange-connected to the filter box (3), and the ash collection hopper (22) is slidably connected to the filter box (3).
4. The coke oven gas primary cooler spray purification device according to claim 3, characterized in that: The limiting block (23) is screwed to the filter box (3) and the ash collection hopper (22). The coarse filter plate (21), the fine filter plate (18) and the adsorption plate (20) are slidably connected to the limiting block (23). The top of the coarse filter plate (21), the fine filter plate (18) and the adsorption plate (20) are all provided with handles (2).
5. The coke oven gas primary cooler spray purification device according to claim 1, characterized in that: The limiting slide rail (7) is screwed to the spray box (1), and the horizontal plate (8) and the grid plate (13) are slidably connected to the spray box (1).
6. The coke oven gas primary cooler spray purification device according to claim 1, characterized in that: The activated carbon particles (6) are connected to the horizontal plate (8) through a slot, the condensation circulation pipe (9) is connected to the horizontal grid slot of the grid plate (13), and the guide plate (12) is inclined at 60 degrees.
7. The coke oven gas primary cooler spray purification device according to claim 1, characterized in that: The water outlet pipe (16) is inserted into the spray box (1), the one-way solenoid valve (17) is connected to the flange of the water outlet pipe (16), the first connecting pipe (10) and the second connecting pipe (15) are both inserted into the spray box (1), the first spray head (14) is inserted into the first connecting pipe (10), and the second spray head (11) is inserted into the second connecting pipe (15).