Active coke biological membrane adsorption reactor

Abstract

The utility model discloses and provides an active coke biofilm adsorption reactor, which comprises a plurality of groups of reaction tanks, one end of a water inlet pipe is connected with a first flow guide pipe, two ends of the first flow guide pipe are connected with second flow guide pipes, two ends of each second flow guide pipe are connected with eight-claw water distributors, one side of each eight-claw water distributor is connected with a water absorption cover, and the other side of each eight-claw water distributor is connected with a water storage tank. The bottom end of the water absorption cover is connected with a support frame, the support frame is fixedly connected with the inner wall of the bottom end of the reaction tank, a filter bed is arranged in the reaction tank, the top end of the reaction tank is fixedly provided with a fixed seat, and the outer surface of the fixed seat is provided with a feeding pipe. The water flow distribution and the reaction efficiency in the reactor are improved, the diameter of a lifting pipeline is increased, the equipment cleaning height is increased, cleaning is more efficient, and the cleaning time and the maintenance cost are reduced.

Description

Technical Field

[0001] The utility model relates to the technical field of activated coke biofilm adsorption, in particular to an activated coke biofilm adsorption reactor. Background Art

[0002] With the rapid development of industrialization and urbanization, water pollution is becoming increasingly serious, among which non-biodegradable organic pollutants (COD) have become a major challenge in the field of water treatment. Traditional biological treatment methods are often ineffective for such pollutants, so the development of new and efficient adsorption materials and reactors has become a research hotspot.

[0003] Moving Bed Biofilm Reactor (MBBR) is an emerging water treatment technology that has attracted widespread attention due to its high efficiency, low energy consumption, and easy maintenance. This technology mainly uses porous carbonaceous materials such as activated coke as adsorption media, and achieves effective adsorption and removal of difficult-to-biodegrade COD through full contact and mixing with sewage.

[0004] Most traditional moving bed adsorption reactors are improved based on the principle of continuous flow activated sand filter, integrating filtration and adsorption functions. However, in practical applications, traditional reactor designs often have some problems, such as insufficient contact between the adsorption medium and sewage, uneven flow inside the reactor, etc. These problems limit the adsorption efficiency and stability of the reactor. Utility Model Content

[0005] (I) Purpose of the utility model

[0006] In view of this, the purpose of the present invention is to provide an activated coke biofilm adsorption reactor to solve the problems raised in the above background.

[0007] (II) Technical solution

[0008] An activated coke biofilm adsorption reactor comprises a plurality of reaction pools, wherein the plurality of reaction pools are operated in parallel and can be operated independently, the inner walls of the plurality of reaction pools are all provided with water inlet pipes, and one end of the water inlet pipe is connected to a first flow guide pipe, both ends of the first flow guide pipe are both connected to a second flow guide pipe, and both ends of the second flow guide pipe are both connected to an eight-claw water distributor, one side of the eight-claw water distributor is connected to a water absorption hood, and the bottom end of the water absorption hood is connected to a support frame, the support frame is fixedly connected to the inner wall of the bottom end of the reaction pool, and a filter bed is arranged inside the reaction pool, a fixing seat is fixedly installed on the top of the reaction pool, and a feeding pipe is arranged on the outer surface of the fixing seat.

[0009] Preferably, a flange is installed at one end of the feeding pipe, and a plurality of distribution pipes are connected to the bottom end of the feeding pipe.

[0010] Preferably, multiple groups of the reaction tanks are fixedly mounted with a fixing frame on the inner wall at the top, and multiple groups of lifters are installed on the outer surface of the fixing frame, one end of the multiple groups of lifters is connected to a stripping pipe, and one end of the stripping pipe is connected to a connecting suction cup, and one end of the connecting suction cup is connected to an octopus water distributor.

[0011] Preferably, a plurality of aeration tubes are provided at the bottom end of the water absorption hood.

[0012] Preferably, a reinforcement frame is fixedly mounted on the outer surface of the first flow guide pipe.

[0013] Preferably, the bottom ends of the multiple groups of lifters are all connected to a delivery pipe.

[0014] Preferably, the filter bed is composed of porous carbonaceous filter material.

[0015] It can be seen from the above technical solutions that the present application has the following beneficial effects:

[0016] 1. The utility model uses an eight-claw water distributor to make the water distribution area larger and more uniform, thereby improving the water flow distribution and reaction efficiency in the reactor, and increasing the diameter of the lifting pipeline and the equipment cleaning height, making cleaning more efficient and reducing cleaning time and maintenance costs.

[0017] 2. The utility model not only prevents the filter material from caking through the aeration pipe, but also provides a micro-oxygen environment for the growth of biofilm on the activated coke. The micro-oxygen environment is conducive to the growth and activity maintenance of the biofilm, and further degrades the adsorbed COD through biodegradation. The growth and activity maintenance of the biofilm can prolong the biological residence time and improve the pollutant removal efficiency.

[0018] 3. The utility model eliminates the need for secondary pouring of the pool bottom through the water absorption hood guide device, simplifies the construction process and reduces civil engineering costs.

[0019] 4. The utility model can accurately monitor and regulate the reactor operating parameters through intelligent automatic control to ensure the treatment effect and stability, reduce the difficulty of operation, and improve the operating efficiency and management level of the system.

[0020] 5. The utility model can operate individually or in parallel through the reaction pool to adapt to different treatment needs. This flexibility increases the reliability and efficiency of the treatment process. BRIEF DESCRIPTION OF THE DRAWINGS

[0021] Figure 1 It is a schematic diagram of the three-dimensional structure of the utility model;

[0022] Figure 2 This is a three-dimensional cross-sectional structural schematic diagram of the utility model;

[0023] Figure 3This is a schematic diagram of the cross-sectional structure of the utility model;

[0024] Figure 4 For this utility model Figure 2 The enlarged schematic diagram at A in the middle;

[0025] Figure 5 For this utility model Figure 2 Enlarged schematic diagram of point B in the middle.

[0026] In the figure: 1, reaction tank; 2, fixing seat; 3, feeding pipe; 4, fixing frame; 5, lifting device; 6, water inlet pipe; 7, first guide pipe; 8, second guide pipe; 9, eight-claw water distributor; 711, reinforcement frame; 511, stripping pipe; 512, connecting suction cup; 513, water absorption hood; 514, supporting frame; 211, filter bed; 212, conveying pipe; 311, flange; 312, distribution pipe; 111, aeration pipe. DETAILED DESCRIPTION

[0027] The following description is merely exemplary in nature and is not intended to limit the present disclosure, application, and use. It should be understood that in all of these figures, the same or similar reference numerals indicate the same or similar parts and features. The various drawings only schematically represent the concepts and principles of the embodiments of the present disclosure, and do not necessarily show the specific dimensions and proportions of the various embodiments of the present disclosure. Specific parts in specific drawings may be exaggerated to illustrate the relevant details or structures of the embodiments of the present disclosure.

[0028] See also Figure 1-5 , an embodiment provided by the utility model:

[0029] An activated coke biofilm adsorption reactor comprises a plurality of reaction tanks 1, wherein the plurality of reaction tanks 1 are operated in parallel and can be operated independently, wherein the inner walls of the plurality of reaction tanks 1 are all provided with a water inlet pipe 6, and one end of the water inlet pipe 6 is connected to a first flow guide pipe 7, both ends of the first flow guide pipe 7 are both connected to a second flow guide pipe 8, and both ends of the second flow guide pipe 8 are both connected to an octopus water distributor 9, one side of the octopus water distributor 9 is connected to a water absorption hood 513, and the bottom end of the water absorption hood 513 is connected to a support frame 514, the support frame 514 is fixedly connected to the inner wall of the bottom end of the reaction tank 1, and a filter bed 211 is arranged inside the reaction tank 1, a fixing seat 2 is fixedly installed on the top of the reaction tank 1, and a feeding pipe 3 is arranged on the outer surface of the fixing seat 2.

[0030] Furthermore, a flange 311 is installed at one end of the feeding pipe 3, and a plurality of distribution pipes 312 are connected to the bottom end of the feeding pipe 3. The flange 311 is connected to the feeding tank through a pipeline. By installing the flange 311 at one end of the feeding pipe 3, it is ensured that the connection between the feeding pipe 3 and the feeding tank is stable and not easy to loosen. At the same time, the design of the flange 311 also provides good sealing, prevents leakage of materials during transportation, and ensures the safe operation of the reactor. The design of the plurality of distribution pipes 312 also makes the distribution of materials inside the reactor more controllable, which is convenient for operators to adjust and optimize.

[0031] Furthermore, a fixing frame 4 is fixedly installed on the inner wall of the top of each of the multiple reaction pools 1, and a plurality of lifters 5 are installed on the outer surface of the fixing frame 4, one end of the plurality of lifters 5 is connected to a stripping tube 511, and one end of the stripping tube 511 is connected to a connecting suction cup 512, and one end of the connecting suction cup 512 is connected to an octopus water distributor 9, and the octopus water distributor 9 is interconnected with the inner wall of the stripping tube 511 and the water absorption hood 513. This design enables saturated adsorption media such as activated coke to be easily lifted and cleaned online through the stripping tube, which greatly simplifies the operation process.

[0032] Furthermore, a plurality of aeration tubes 111 are provided at the bottom end of the water absorbing hood 513, and the plurality of aeration tubes 111 effectively prevent the filter material from being compacted and maintain good filtering performance of the filter material.

[0033] Furthermore, a reinforcement frame 711 is fixedly installed on the outer surface of the first flow guide pipe 7, which enhances its structural stability and prevents the pipe from being deformed or damaged due to water flow impact or other external forces.

[0034] Furthermore, the bottom ends of the multiple groups of elevators 5 are all connected to a conveying pipe 212, and the conveying pipe 212 discharges the material to a vibrating screen, and after being vibrated and dehydrated by the vibrating screen, it is loaded into a ton bag. Through effective dehydration treatment and storage methods, the impact of the adsorption medium on the environment during transportation and storage can be reduced, and energy consumption and costs are also reduced.

[0035] Furthermore, the filter bed 211 is composed of porous carbonaceous filter material, which has extremely high specific surface area and porosity, and can provide a large number of adsorption sites, thereby effectively adsorbing pollutants such as organic matter and heavy metal ions in water. This makes the filter bed 211 perform well in treating sewage and can achieve a high removal rate and purification effect.

[0036] Working principle: First, in the reaction tank 1, the sewage first enters through the water inlet pipe 6, and then is guided by the first guide pipe 7 and the second guide pipe 8, and finally evenly distributed to the eight-claw water distributor 9. The design of the eight-claw water distributor 9 ensures the uniform distribution of water flow in the reaction tank, so that the sewage can fully contact with the adsorption medium such as activated coke in the reaction tank. The water flows from bottom to top through the filter bed 211. During this process, pollutants such as COD that are difficult to biodegrade are adsorbed and removed by the activated coke, thereby achieving purification. The filtered clean water gathers at the top of the reaction tank and overflows through the overflow port to complete the treatment process. As the filtration process proceeds, the adsorption medium such as activated coke at the bottom of the reaction tank will gradually become saturated. In order to maintain the continuous and efficient operation of the reactor, these saturated adsorption media need to be cleaned and regenerated regularly. At this time, by starting the lifter 5 on the fixed frame 4, the adsorption medium is lifted to the stripping pipe 511 and connected to the eight-claw water distributor 9 through the connecting suction cup 512. The design of the stripping pipe 511 allows the adsorption medium to be cleaned online by introducing a medium such as air or steam to remove pollutants attached thereto. The cleaned sewage is collected by the water absorbing hood 513 and discharged through the conveying pipe 212. The cleaned adsorption medium is then transported to the vibrating screen through the conveying pipe 212 for further dehydration. The vibrating screen removes excess water from the surface of the adsorption medium through vibration and packs it into a ton bag for subsequent use or disposal.

[0037] It is obvious to those skilled in the art that the present invention is not limited to the details of the exemplary embodiments described above, and that the present invention can be implemented in other specific forms without departing from the spirit or essential features of the present invention. Therefore, the embodiments should be regarded as exemplary and non-restrictive from any point of view, and the scope of the present invention is defined by the appended claims rather than the above description, and it is intended that all changes falling within the meaning and scope of the equivalent elements of the claims be included in the present invention. Any reference numeral in a claim should not be regarded as limiting the claim to which it relates.

Claims

1. An activated coke biofilm adsorption reactor, comprising a plurality of reaction tanks (1), characterized in that: Multiple groups of reaction pools (1) are operated in parallel, and multiple groups of reaction pools (1) can be operated independently. The inner walls of the multiple groups of reaction pools (1) are all provided with water inlet pipes (6), and one end of the water inlet pipe (6) is connected to a first flow guide pipe (7), both ends of the first flow guide pipe (7) are connected to a second flow guide pipe (8), and both ends of the second flow guide pipe (8) are connected to an eight-claw water distributor (9), one side of the eight-claw water distributor (9) is connected to a water absorption cover (513), and the bottom end of the water absorption cover (513) is connected to a support frame (514), the support frame (514) is fixedly connected to the inner wall of the bottom end of the reaction pool (1), and a filter bed (211) is arranged inside the reaction pool (1), and a fixing seat (2) is fixedly installed at the top of the reaction pool (1), and a feeding pipe (3) is arranged on the outer surface of the fixing seat (2).

2. The activated coke biofilm adsorption reactor according to claim 1, characterized in that: A flange (311) is installed at one end of the feeding pipe (3), and a plurality of distribution pipes (312) are connected to the bottom end of the feeding pipe (3).

3. The activated coke biofilm adsorption reactor according to claim 1, characterized in that: A fixing frame (4) is fixedly mounted on the inner wall of the top of each of the plurality of reaction tanks (1), and a plurality of lifters (5) are mounted on the outer surface of the fixing frame (4), one end of each of the plurality of lifters (5) is connected to a stripping tube (511), and one end of the stripping tube (511) is connected to a connecting suction cup (512), and one end of the connecting suction cup (512) is connected to an octagonal water distributor (9).

4. The activated coke biofilm adsorption reactor according to claim 1, characterized in that: A plurality of aeration pipes (111) are provided at the bottom end of the water absorption hood (513).

5. The activated coke biofilm adsorption reactor according to claim 1, characterized in that: A reinforcement frame (711) is fixedly mounted on the outer surface of the first flow guide pipe (7).

6. The activated coke biofilm adsorption reactor according to claim 3, characterized in that: The bottom ends of the multiple groups of lifters (5) are all connected to a delivery pipe (212).

7. The activated coke biofilm adsorption reactor according to claim 1, characterized in that: The filter bed (211) is composed of porous carbonaceous filter material.

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