A highly efficient activated carbon adsorption device with recyclable desorption capability
By introducing an oxidant tank and a cleaning device into the activated carbon adsorption equipment, room temperature desorption and recycling of activated carbon can be achieved, solving the problems of high regeneration cost and pollution of traditional activated carbon, and improving equipment efficiency and environmental friendliness.
Patent Information
- Authority / Receiving Office
- CN · China
- Patent Type
- Utility models(China)
- Current Assignee / Owner
- 江苏众明华鼎环保科技有限公司
- Filing Date
- 2025-05-07
- Publication Date
- 2026-06-30
AI Technical Summary
Traditional activated carbon adsorption equipment is difficult to regenerate efficiently after saturation, resulting in high costs and potential secondary pollution. Existing regeneration methods are energy-intensive or may damage the structure.
The design combines an oxidant tank with an adsorption tower. The oxidant is evenly sprayed onto activated carbon by a pressurized pump to carry out chemical desorption. The regeneration process is carried out at room temperature, and the system is combined with a cleaning device to achieve recycling.
It reduces regeneration energy consumption, avoids damage to the activated carbon structure caused by high temperatures, increases the number of times activated carbon can be reused and its adsorption performance, reduces secondary pollution, and saves water resources.
Smart Images

Figure CN224422905U_ABST
Abstract
Description
Technical Field
[0001] This utility model specifically relates to the field of activated carbon adsorption equipment technology, and more specifically to a highly efficient activated carbon adsorption equipment with cyclic desorption capability. Background Technology
[0002] Against the backdrop of an increasingly severe environmental protection situation, industrial waste gas treatment has become a critical issue that urgently needs to be addressed. Volatile organic compounds (VOCs), as a significant component of air pollutants, have a wide range of sources, covering numerous industries such as chemicals, coating, printing, and electronics. The VOCs emitted by these industries have complex and diverse concentrations and compositions, posing a serious threat to the ecological environment and human health.
[0003] Activated carbon adsorption technology is widely used in VOCs treatment due to its high efficiency and economy. Activated carbon has a rich microporous structure and a large specific surface area, which can effectively adsorb pollutants in waste gas and achieve purification. However, in traditional activated carbon adsorption equipment, the adsorption performance will significantly decrease when the activated carbon becomes saturated. Directly replacing the activated carbon is not only costly, but the discarded activated carbon may also become a new source of pollution. Traditional activated carbon regeneration methods, such as thermal regeneration, are energy-intensive, require sophisticated equipment, and are prone to damaging the activated carbon structure. Conventional chemical regeneration is prone to generating secondary pollution. Therefore, realizing the regeneration and recycling of activated carbon is the key to improving the efficiency of adsorption equipment, reducing operating costs, and reducing environmental pollution. Utility Model Content
[0004] The purpose of this invention is to provide a highly efficient activated carbon adsorption device with cyclic desorption. By installing the desorption device and the cleaning device with the adsorption tower body, the activated carbon adsorption device can achieve cyclic desorption while reducing secondary pollution after desorption, thereby solving the technical problems mentioned in the background art.
[0005] To achieve the above objectives, this utility model provides the following technical solution:
[0006] A highly efficient activated carbon adsorption device with cyclic desorption capability, comprising:
[0007] The adsorption tower body is connected to a desorption device and a cleaning device on its two sides, respectively.
[0008] The desorption device includes an oxidant tank with a maintenance port at the top, a level gauge at one end, a discharge port and a replenishment port on the other side, oxidant tank support legs at the bottom, and a pressure pump at the other end. The other end of the pressure pump is connected to an upper spray pipe, the upper end of which is connected to an upper fixed valve. The upper fixed valve is fixedly connected to one side of the tower body, and the inner side of the upper fixed valve is connected to an upper liquid distribution pipe. The upper liquid distribution pipe is equipped with multiple spiral nozzles.
[0009] As a further technical solution of this utility model, the bottom of the tower body is provided with adsorption tower legs, and an air inlet is provided on one side of the lower end of the tower body. On the same side as the air inlet, a number of square openings are regularly arranged. Each square opening is provided with a drawer that is slidably connected, and each drawer is provided with an activated carbon adsorption plate.
[0010] As a further technical solution of this utility model, the top of the tower body is provided with an air outlet and the bottom is provided with a drain outlet. The drain outlet is fixedly connected to the water inlet and the water inlet is fixedly connected to the circulation box at the bottom.
[0011] As a further technical solution of this utility model, the upper part of the circulation box is provided with an inclined guide plate, the other end of the guide plate is fixedly connected to the double-layer activated carbon filter plate, and the bottom of the double-layer activated carbon filter plate has a sedimentation cavity; the bottom of the guide plate is provided with an L-shaped sedimentation plate, and a water passage is left between the guide plate and the L-shaped sedimentation plate. The L-shaped sedimentation plate is located at the upper end of the sedimentation cavity and is located inside the circulation box.
[0012] As a further technical solution of this utility model, a discharge port is fixedly installed on one side of the circulation box, and a sliding plate is slidably connected to the discharge port; one end of the circulation box is connected to a water pump, the other end of the water pump is connected to a lower spray pipe, the upper end of the lower spray pipe is connected to a lower fixed valve, the lower fixed valve is fixedly connected to one side of the tower body, the inner side of the lower fixed valve is connected to a lower liquid distribution pipe, and the lower liquid distribution pipe is provided with multiple adjustable nozzles.
[0013] Compared with the prior art, the beneficial effects of this utility model are:
[0014] In this invention, once the activated carbon adsorption plate is saturated, the desorption device is activated. The oxidant in the oxidant tank is pressurized by a pressure pump and delivered to the upper spray pipe. Then, it is evenly sprayed onto the activated carbon adsorption plate through multiple spiral nozzles on the upper liquid distribution pipe. The oxidant reacts chemically with the pollutants adsorbed on the activated carbon, oxidizing and decomposing the pollutants, thereby achieving the desorption and regeneration of the activated carbon. The oxidant desorption method can be carried out at room temperature, which significantly reduces energy consumption compared to thermal regeneration. It can also effectively avoid the damage to the activated carbon structure caused by high temperature, increase the number of times the activated carbon can be reused and its adsorption performance, thereby improving the overall processing efficiency of the adsorption equipment. At the same time, the reaction products of the oxidant desorption are clean, reducing secondary pollution.
[0015] In this invention, the maintenance port at the top of the oxidant tank facilitates internal maintenance; the level gauge can monitor the oxidant level in real time, allowing for timely replenishment of new oxidant through the replenishment port; the discharge port is used to discharge waste oxidant; and the adsorption tower body adopts a drawer-type structure to install activated carbon adsorption plates, facilitating the replacement and maintenance of activated carbon.
[0016] This invention relates to a circulating water system in a cleaning device. Through structures such as a guide plate, a double-layer activated carbon filter plate, an L-shaped sedimentation plate, a sedimentation chamber, a discharge port, and a sliding plate, the system achieves the recycling of cleaning water, saving water and reducing wastewater discharge. The adjustable nozzles in the cleaning device can adjust the spray intensity according to actual needs, ensuring cleaning effectiveness while improving resource utilization. Attached Figure Description
[0017] Figure 1 This is a three-dimensional structural diagram of the present invention.
[0018] Figure 2 This utility model Figure 1 Top view.
[0019] Figure 3 This utility model Figure 2 Top view.
[0020] Figure 4 This utility model Figure 3 A partial sectional view.
[0021] Figure 5 This utility model Figure 4 A bottom view.
[0022] Figure 6 This utility model Figure 5 The right view.
[0023] Figure 7 This utility model Figure 5 A magnified view of a portion of the image.
[0024] Figure 8 This utility model Figure 6 A magnified view of a portion of the image.
[0025] In the diagram: 1-Adsorption tower body, 2-Desorption device, 3-Cleaning device;
[0026] 11-Tower body, 12-Adsorption tower support leg, 13-Air inlet, 14-Square opening, 15-Drawer, 16-Air outlet, 17-Activated carbon adsorption plate, 18-Drain outlet;
[0027] 21-Oxidizer tank, 22-Maintenance port, 23-Level gauge, 24-Oxidizer tank support leg, 25-Discharge port, 26-Replenishment port, 27-Pressure pump, 28-Upper spray pipe, 29-Upper fixed valve, 210-Upper liquid distribution pipe, 211-Spiral nozzle;
[0028] 31-Inlet, 32-Circulation tank, 33-Guide plate, 34-Double-layer activated carbon filter plate, 35-L-sediment plate, 36-Drain outlet, 37-Sliding plate, 38-Water pump, 39-Lower fixed valve, 310-Lower liquid distribution pipe, 311-Adjustable nozzle, 312-Sedimentation chamber, 313-Lower spray pipe. Detailed Implementation
[0029] The technical solutions of the present utility model will be clearly and completely described below with reference to the accompanying drawings of the embodiments. Obviously, the described embodiments are only some embodiments of the present utility model, and not all embodiments. Based on the embodiments of the present utility model, all other embodiments obtained by those of ordinary skill in the art without creative effort are within the protection scope of the present utility model.
[0030] Please see Figure 1-8 In this embodiment of the present invention, a high-efficiency activated carbon adsorption device with cyclic desorption includes an adsorption tower body 1, the two sides of which are respectively connected to a desorption device 2 and a cleaning device 3.
[0031] The desorption device 2 includes an oxidant tank 21, which has a maintenance port 22 at the top, a level gauge 23 at one end, a discharge port 25 and a replenishment port 26 on one side, an oxidant tank support leg 24 at the bottom, and a pressure pump 27 at the other end. The other end of the pressure pump 27 is connected to an upper spray pipe 28, the upper end of the upper spray pipe 28 is connected to an upper fixed valve 29, the upper fixed valve 29 is fixedly connected to one side of the tower body 11, and the inner side of the upper fixed valve 29 is connected to an upper liquid distribution pipe 210. The upper liquid distribution pipe 210 is equipped with multiple spiral nozzles 211.
[0032] By adopting the above technical solution, in this utility model, when the activated carbon adsorption plate 17 is saturated, the desorption device 2 is started. The oxidant in the oxidant tank 21 is pressurized by the pressure pump 27 and transported to the upper spray pipe 28. Then, it is evenly sprayed onto the activated carbon adsorption plate 17 through multiple spiral nozzles 211 on the upper liquid distribution pipe 210. The oxidant reacts chemically with the pollutants adsorbed on the activated carbon, oxidizing and decomposing the pollutants, thereby realizing the desorption and regeneration of the activated carbon. The oxidant desorption method can be carried out at room temperature, which greatly reduces energy consumption compared with thermal regeneration. It can also effectively avoid the damage of high temperature to the activated carbon structure, increase the number of times the activated carbon can be reused and the adsorption performance, thereby improving the overall processing efficiency of the adsorption equipment. At the same time, the reaction products of the oxidant desorption are clean, reducing secondary pollution.
[0033] In this embodiment, the bottom of the tower body 11 is provided with an adsorption tower support leg 12, and an air inlet 13 is provided on one side of the lower end of the tower body 11. On the same side as the air inlet 13, a plurality of square openings 14 are also regularly provided. Each square opening 14 is provided with a drawer 15 that is slidably connected, and each drawer 15 is provided with an activated carbon adsorption plate 17.
[0034] By adopting the above technical solution, the maintenance port 22 at the top of the oxidant tank 21 facilitates internal maintenance; the level gauge 23 can monitor the oxidant level in real time, and new oxidant can be added in time through the replenishment port 26; the discharge port 25 is used to discharge waste oxidant; the adsorption tower body 11 adopts a drawer-type structure 15 to install the activated carbon adsorption plate 17, which facilitates the replacement and maintenance of activated carbon.
[0035] In this embodiment, the top of the tower body 11 is provided with an air outlet 16 and the bottom is provided with a drain outlet 18. The drain outlet 18 is fixedly connected to the water inlet 31, and the water inlet 31 is fixedly connected to the circulation box 32 at the bottom.
[0036] The upper part of the circulation box 32 is provided with an inclined guide plate 33. The other end of the guide plate 33 is fixedly connected to the double-layer activated carbon filter plate 34. The bottom of the double-layer activated carbon filter plate 34 has a sedimentation chamber 312. The bottom of the guide plate 33 is provided with an L-sedimentation plate 35, and a water passage is provided between the guide plate 33 and the L-sedimentation plate 35. The L-sedimentation plate 35 is located at the upper end of the sedimentation chamber 312 and is located inside the circulation box 32.
[0037] The circulation tank 32 is fixedly installed with a discharge port 36 on one side, and a sliding plate 37 is slidably connected to the discharge port 36; one end of the circulation tank 32 is connected to a water pump 38, the other end of the water pump 38 is connected to a lower spray pipe 313, the upper end of the lower spray pipe 313 is connected to a lower fixed valve, the lower fixed valve is fixedly connected to one side of the tower body 11, the inner side of the lower fixed valve is connected to a lower liquid distribution pipe 310, and the lower liquid distribution pipe 310 is provided with multiple adjustable nozzles 311.
[0038] By adopting the above technical solution, the circulating water system in the cleaning device 3, through the structure of the guide plate 33, double-layer activated carbon filter plate 34, L-sediment plate 35, sedimentation chamber 312, discharge port 36 and sliding plate 37, realizes the recycling of cleaning water, saves water and reduces sewage discharge; the adjustable nozzle 311 in the cleaning device can adjust the spray intensity according to actual needs, ensuring the cleaning effect while improving resource utilization.
[0039] The working principle of this utility model is as follows: When the activated carbon adsorption plate 17 is saturated, the desorption device 2 is activated. The oxidant in the oxidant tank 21 is pressurized by the pressure pump 27 and transported to the upper spray pipe 28. Then, it is evenly sprayed onto the activated carbon adsorption plate 17 through multiple spiral nozzles 211 on the upper liquid distribution pipe 210. The oxidant reacts chemically with the pollutants adsorbed on the activated carbon, oxidizing and decomposing the pollutants, thereby achieving the desorption and regeneration of the activated carbon. The oxidant desorption method can be carried out at room temperature, which significantly reduces energy consumption compared to thermal regeneration. It can also effectively avoid the damage to the activated carbon structure caused by high temperature, increase the number of times the activated carbon can be reused and the adsorption performance, thereby improving the overall processing efficiency of the adsorption equipment. At the same time, the reaction products of the oxidant desorption are clean, reducing secondary pollution.
[0040] The maintenance port 22 at the top of the oxidant tank 21 facilitates internal maintenance; the level gauge 23 can monitor the oxidant level in real time, and new oxidant can be added in time through the replenishment port 26; the discharge port 25 is used to discharge waste oxidant; the adsorption tower body 11 adopts a drawer-type structure 15 to install the activated carbon adsorption plate 17, which facilitates the replacement and maintenance of activated carbon.
[0041] After desorption is completed, the cleaning device 3 is started. The water in the circulation tank 32 is sprayed and cleaned by the water pump 38 through the lower spray pipe 313, the lower liquid distribution pipe 310 and the multiple adjustable nozzles 311 above to remove residual oxidants and decomposition products and other impurities. The cleaned water flows back to the circulation tank 32 through the drain port 18 at the bottom of the tower body 11. Inside the circulation tank 32, the inclined guide plate 33 guides the returned water to the double-layer activated carbon filter plate 34 to further filter impurities in the water. The purified water can be recycled. The L sedimentation plate 35 cooperates with the guide plate 33 to make impurities deposit in the sedimentation chamber 312, which can be cleaned periodically through the discharge port 36 and the sliding plate 37.
[0042] The circulating water system in the cleaning device 3, through structures such as the guide plate 33, the double-layer activated carbon filter plate 34, the L-sediment plate 35, the sedimentation chamber 312, the discharge port 36, and the sliding plate 37, realizes the recycling of cleaning water, saving water and reducing sewage discharge; the adjustable nozzle 311 in the cleaning device can adjust the spray intensity according to actual needs, ensuring the cleaning effect while improving resource utilization.
[0043] It will be apparent to those skilled in the art that this invention is not limited to the details of the exemplary embodiments described above, and that it can be implemented in other specific forms without departing from the spirit or essential characteristics of this invention. Therefore, the embodiments should be considered illustrative and non-limiting in all respects, and the scope of this invention is defined by the appended claims rather than the foregoing description. Thus, it is intended that all variations falling within the meaning and scope of equivalents of the claims be included within this invention. No reference numerals in the claims should be construed as limiting the scope of the claims.
[0044] Furthermore, it should be understood that although this specification describes embodiments, not every embodiment contains only one independent technical solution. This narrative style of the specification is merely for clarity. Those skilled in the art should consider the specification as a whole, and the technical solutions in each embodiment can also be appropriately combined to form other embodiments that can be understood by those skilled in the art.
Claims
1. A high efficiency activated carbon adsorption apparatus that is cyclically desorbable, characterized by: include The adsorption tower body (1) is connected to the desorption device (2) and the cleaning device (3) on both sides respectively. The desorption device (2) includes an oxidant tank (21), which has a maintenance port (22) at the top, a level gauge (23) at one end, a discharge port (25) and a replenishment port (26) on one side, an oxidant tank support leg (24) at the bottom, and a pressure pump (27) at the other end. The other end of the pressure pump (27) is connected to the upper spray pipe (28), the upper end of the upper spray pipe (28) is connected to the upper fixed valve (29), the upper fixed valve (29) is fixedly connected to one side of the tower body (11), the inner side of the upper fixed valve (29) is connected to the upper liquid distribution pipe (210), and the upper liquid distribution pipe (210) is provided with multiple spiral nozzles (211).
2. The high-efficiency activated carbon adsorption device with cyclic desorption according to claim 1, characterized in that: The bottom of the tower body (11) is provided with adsorption tower support legs (12), and an air inlet (13) is provided on one side of the lower end of the tower body (11). On the same side as the air inlet (13), there are also a number of square openings (14) arranged in a regular pattern. Each square opening (14) is provided with a drawer (15) that is slidably connected, and each drawer (15) is provided with an activated carbon adsorption plate (17).
3. The high-efficiency activated carbon adsorption device with cyclic desorption according to claim 2, characterized in that: The tower body (11) is provided with an air outlet (16) at the top and a drain outlet (18) at the bottom. The drain outlet (18) is fixedly connected to the water inlet (31), and the water inlet (31) is fixedly connected to the circulation box (32) at the bottom.
4. The high-efficiency activated carbon adsorption device with cyclic desorption according to claim 3, characterized in that: The upper part of the circulation box (32) is provided with an inclined guide plate (33), and the other end of the guide plate (33) is fixedly connected to the double-layer activated carbon filter plate (34). The bottom of the double-layer activated carbon filter plate (34) has a sedimentation chamber (312). The bottom of the guide plate (33) is provided with an L sedimentation plate (35), and a water passage is left between the guide plate (33) and the L sedimentation plate (35). The L sedimentation plate (35) is located at the upper end of the sedimentation chamber (312) and is located inside the circulation box (32).
5. The high-efficiency activated carbon adsorption device with cyclic desorption according to claim 4, characterized in that: The circulation tank (32) is fixedly installed with a discharge port (36) on one side, and a sliding plate (37) is slidably connected to the discharge port (36); one end of the circulation tank (32) is connected to a water pump (38), the other end of the water pump (38) is connected to a lower spray pipe (313), the upper end of the lower spray pipe (313) is connected to a lower fixed valve, the lower fixed valve is fixedly connected to one side of the tower body (11), the inner side of the lower fixed valve is connected to a lower liquid distribution pipe (310), and the lower liquid distribution pipe (310) is provided with multiple adjustable nozzles (311).