Rapid screening equipment based on low-temperature anaerobic ammonia oxidation particles

Through the combination of fixed filter tube and mechanical particle selection mechanism, the blockage and low efficiency of the mesh panel screening equipment in low-temperature environment is solved, efficient particle screening and dehydration is achieved, equipment cost and operation risks are reduced, and the treatment needs of low-temperature anaerobic ammonia oxidation particles are adapted.

CN120479037APending Publication Date: 2025-08-15NANJING UNIV
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Patent Information

Application Number
CN202510832656.8
Authority / Receiving Office
CN · China
Patent Type
Applications(China)
Current Assignee / Owner
Filing Date
2025-06-20
Publication Date
2025-08-15

AI Technical Summary

Technical Problem

The existing mesh panel screening equipment is prone to problems such as freezing and blocking of the flushing water system in low temperature environments, and the interception effect of anaerobic ammonia oxidized particles is poor, resulting in high operating costs and low efficiency of the equipment, and it is difficult to effectively remove particles attached to the filter, affecting the normal operation of the equipment.

Method used

The fixed filter tube structure is adopted, combining the mechanical particle preferential mechanism and the siphon slag discharge mechanism to prevent the grid slag and particles from aggregating and winding through vertical shearing motion. The filter hole dynamic adjustment mechanism is used to adapt particles of different particle size specifications, and compress and dehydrate with the particle separation mechanism.

Benefits of technology

It reduces equipment costs and operating risks, improves equipment stability and processing efficiency, avoids the problem of freezing of the flushing water system, adapts to the treatment needs of anaerobic ammonia oxidation particles in low-temperature environments, reduces wear and loss, and improves the service life of the equipment.

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Abstract

The invention discloses rapid screening equipment based on low-temperature anaerobic ammonia oxidation particles. The rapid screening equipment comprises a screening supporting mechanism fixed in a pretreatment circulation channel, a filter pipe combination mechanism arranged in the screening supporting mechanism, a siphon deslagging mechanism connected with the filter pipe combination mechanism and a particle separation mechanism. The screening supporting mechanism comprises a screening supporting containing shell which is fixed in the pretreatment circulation channel and is provided with an upward opening, the filter pipe combination mechanism comprises a filter pipe combination containing shell which is fixed in the screening supporting containing shell, and a plurality of comprehensive filter pipes which are provided with downward openings and are communicated with the outside are fixed at the bottom in the filter pipe combination containing shell; a plurality of comprehensive filtering micropores which are communicated inside and outside are formed in the side wall of the comprehensive filtering pipe; the screening equipment adopts a fixed filter pipe structure, so that the screen surface of a filter screen for conventional screen plate screening is reduced, the equipment cost is reduced, meanwhile, movement abrasion is avoided, and the operation stability of the equipment is improved.
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Description

Technical Field

[0001] The present invention relates to the technical field of mud-water mixture treatment, in particular to a rapid screening device based on low-temperature anaerobic ammonia oxidation particles. Background Art

[0002] In order to adapt to the increasing requirements of the current miniaturization of mud-water mixture treatment technology, particle screening has also been continuously improved with the improvement of indicators. The mesh screening equipment is one of the main equipment. By providing better interception efficiency, the particles of target particle size in the mud-water mixture can be efficiently separated to achieve the purpose of mud-water mixture particle optimization, which ensures the stable operation of particle-based mud-water mixture treatment process equipment.

[0003] Existing screen screening equipment, whether imported or domestic, generally uses double-sided chains to drive the filter screen assembly for rotational motion to filter the screen residue from the mud-water mixture. After the residue is lifted, the screen residue is carried into the intermediate water tank through gravity, flushing water, and rotating brushes. Since the water and screen residue are in a mixed state, an external high-pressure dewatering press is generally required. Screen screening solves the problem of traditional screening interception efficiency, but its own comprehensive power is much higher than that of traditional screening. At the same time, the amount of flushing water is large. Although reclaimed water is used, the stability and maintenance of the flushing system are very obvious problems due to the high impurities in the water. If a filter is used, the equipment cost will increase. At the same time, it is difficult to eliminate clogging and entanglement problems when flushing the screen, so the design will also add configurations such as cleaning brush rollers and high-pressure particle selectors. This results in further increases in equipment cost and total power.

[0004] In the mud-water mixture treatment process, the low temperature environment and the treatment of anaerobic ammonia oxidation particles have always been the difficulties in the pretreatment link. Traditional screen screening equipment often has many problems when facing particles under low temperature conditions. The original double-sided chain drives the filter screen assembly to perform rotary motion screen screening. In a low temperature environment, the flushing water system is prone to freezing, clogging and other problems, and the retention effect of anaerobic ammonia oxidation particles is not good. The use of flushing water not only increases the operating cost of the equipment, but may also lead to the loss of particles and secondary pollution. At the same time, due to the particularity of anaerobic ammonia oxidation particles, conventional flushing methods are difficult to effectively remove particles attached to the filter screen, which can easily cause the filter screen to be clogged, thereby affecting the normal operation and treatment efficiency of the equipment. Therefore, there is an urgent need for a new filter screen screening purifier for low temperature and anaerobic ammonia oxidation particles to solve the many problems faced by existing equipment under this specific process condition. Summary of the Invention

[0005] The object of the present invention is to provide a rapid screening device based on low-temperature anaerobic ammonia oxidation particles, in which the mechanical particle selection mechanism and the filter pipe mesh plate are vertical shearing movements, effectively preventing the aggregation and entanglement of screen residue and particles.

[0006] To achieve the above object, the present invention provides the following technical solutions:

[0007] A rapid screening device based on low-temperature anaerobic ammonium oxidation particles, comprising a screening support mechanism fixed in a pretreatment flow channel, a filter tube assembly mechanism arranged in the screening support mechanism, a siphon discharge mechanism connected to the filter tube assembly mechanism, and a particle separation mechanism;

[0008] The sub-screening support mechanism includes a sub-screening support housing fixed in the pre-processing flow channel and with an upward opening, and a plurality of sub-screening main inlet pipes connected to the interior of the sub-screening support housing are fixed on the upstream side of the sub-screening support housing;

[0009] The filter tube assembly mechanism includes a filter tube assembly housing fixed in the sub-screening support housing, wherein a plurality of integrated filter tubes with downward openings and communicating with the outside thereof are fixed at the bottom of the filter tube assembly housing;

[0010] The side wall of the integrated filter tube is provided with multiple integrated filter micropores communicating with each other inside and outside;

[0011] A plurality of sub-screening total output pipes connected with the interior of the filter tube combination housing are fixed on the downstream side of the sub-screening support housing.

[0012] Preferably, the integrated filter tube is provided with a particle filtering mechanism, which comprises a particle filtering shearing ring shell slidably connected in the integrated filter tube and with its opening facing downward, wherein the lower end edge of the particle filtering ring shell is a sharp edge structure;

[0013] The top of the integrated filter tube is provided with a vertically penetrating particle optimization drive connection hole, a particle optimization drive push rod is slidably connected in the particle optimization drive connection hole, and a particle optimization shear ring shell is fixed to the lower end of the particle optimization drive push rod;

[0014] The particle-preferred driving push rod extends upward to the outside of the filter tube assembly housing, and a horizontally arranged driving rod linkage plate is fixed to the upper ends of the plurality of particle-preferred driving push rods;

[0015] A particle-preferably driven support frame is fixed in the sieve support accommodating shell, a particle-preferably driven fixed cylinder with an opening facing downward is fixed at the bottom of the particle-preferably driven support frame, a particle-preferably driven sliding cylinder with an opening facing upward is slidably connected in the particle-preferably driven fixed cylinder, and the lower end of the particle-preferably driven sliding cylinder is fixedly connected to a driving rod linkage plate;

[0016] The particle-preferably driven fixed cylinder is provided with a particle-preferably driven telescopic rod for driving the particle-preferably driven sliding cylinder to move up and down.

[0017] Description: The blade structure at the lower edge of the particle-optimizing shearing ring shell is used to shovel off the screenings and particles attached to the inner wall of the integrated filter tube, and the screenings and particles are pushed out from the lower end of the integrated filter tube under the push of the particle-optimizing shearing ring shell.

[0018] Preferably, the integrated filter tube is provided with a filter hole dynamic adjustment mechanism, which includes a filter hole adjustment matching tube slidably connected to the outside of the integrated filter tube, and a plurality of dynamic adjustment matching holes passing through the filter hole adjustment matching tube in its radial direction are provided on the side wall of the filter hole adjustment matching tube;

[0019] The aperture and relative position of the dynamic adjustment matching hole and the integrated filtration micropore are consistent;

[0020] A vertically extending dynamic adjustment push rod is fixed on the filter hole adjustment matching tube, a downward-opening dynamic adjustment fixed cylinder is fixed on the outer side of the integrated filter tube near the top, a dynamic adjustment sliding cylinder with an upward-opening is slidably connected inside the dynamic adjustment fixed cylinder, and the lower end of the dynamic adjustment sliding cylinder is fixedly connected to the dynamic adjustment push rod;

[0021] A dynamic adjustment driving rod for driving the dynamic adjustment sliding cylinder to move up and down is provided in the dynamic adjustment fixing cylinder.

[0022] Description: Each dynamic adjustment matching hole and each integrated filtration micropore can be coaxially aligned and connected at the same time. When the dynamic adjustment matching hole and the integrated filtration micropore are connected, a filtration channel is formed together. By adjusting the overlapping area of the dynamic adjustment matching hole and the integrated filtration micropore, the cross-sectional size of the filtration channel can be adjusted to accommodate particles of various actual particle sizes.

[0023] Preferably, the siphon slag discharge mechanism includes a siphon slag discharge conveying pipe fixed to the bottom of the screening support housing and connected to the interior thereof.

[0024] Description: The siphon discharge mechanism is used to discharge the screenings and particles accumulated at the bottom of the screening support housing, so that the screenings and particles can be further compressed and dehydrated by the particle separation mechanism.

[0025] Preferably, the particle separation mechanism includes a particle separation holding box fixed to one end of the siphon discharge conveying pipe away from the screening support holding shell, the particle separation holding box is a horizontally extending box structure, and a particle separation extrusion slider is slidably fitted in the particle separation holding box;

[0026] A separation mud-water mixture collection is fixed at the bottom of the particle separation holding box, and a plurality of separation mud-water mixture discharge holes connected to the interior of the separation mud-water mixture collection shell are provided on the lower side of the particle separation holding box. A separation mud-water mixture output pipe connected to the interior of the separation mud-water mixture collection shell is fixed at the bottom of the separation mud-water mixture collection shell;

[0027] A compression drive housing is fixed to the end of the particle separation housing box. The end of the particle separation housing box has a compression drive rod connection hole that runs horizontally through and communicates with the interior of the compression drive housing. A particle compression push rod is slidably connected to the compression drive rod connection hole. One end of the particle compression push rod located in the particle separation housing box is fixedly connected to the particle separation extrusion slider.

[0028] A particle compression driving rod for driving the particle compression push rod to move is provided in the compression driving accommodating shell;

[0029] The siphon slag discharge conveying pipe is provided with a siphon slag discharge control valve at one end close to the screening support and accommodation shell and at one end close to the particle separation and accommodation box respectively.

[0030] Description: In the initial state, the particle separation extrusion slider is located inside the particle separation holding box on the side away from the siphon discharge conveying pipe. After the particle separation holding box is filled with screenings and particles, the inner rod of the particle compression driving rod extends and drives the particle separation extrusion slider to move in the particle separation holding box through the particle discharge push rod to squeeze the screenings and particles. The moisture in the screenings and particles will be squeezed out and enter the separation mud and water mixture collection shell through the separation mud and water mixture discharge hole. The mud and water mixture in the separation mud and water mixture collection shell can finally be discharged from the separation mud and water mixture output pipe.

[0031] Preferably, the particle separation holding box has a compressed particle discharge port communicating with the inside and outside on the lower side of one end away from the particle separation extrusion slider, and a particle discharge baffle is slidably connected to the compressed particle discharge port on the lower side of the particle separation holding box;

[0032] A particle discharge driving housing shell is fixed on the upper side of the particle separation housing box and above the compressed particle discharge port. The upper side of the particle separation housing box has a discharge push rod connecting hole that passes vertically through and is connected to the interior of the particle discharge driving housing shell. A particle discharge push rod is slidably connected in the discharge push rod connecting hole. A compressed particle discharge push plate is fixed at one end of the particle discharge push rod in the particle separation housing box. A particle discharge driving rod for driving the particle discharge push rod to move is provided in the particle discharge driving housing shell.

[0033] Description: After the screenings and particles are compressed, they will be located at the compressed particle discharge port. The inner rod of the baffle opening and closing driving rod extends to drive the particle discharge baffle away from the compressed particle discharge port, so that the compressed particle discharge port is in an open state. Then the inner rod of the particle discharge driving rod extends to drive the particle discharge push rod together with the compressed particle discharge push plate to move from top to bottom. Under the push of the compressed particle discharge push plate, the compressed screenings and particles can be pushed out from the compressed particle discharge port.

[0034] Preferably, a monitoring and control mechanism is provided on the inner side wall of the screening support housing, and the monitoring and control mechanism includes multiple water level monitoring sensors fixed on the inner side wall of the screening support housing, and the multiple water level monitoring sensors are evenly dispersed along the vertical direction on the inner side wall of the screening support housing.

[0035] Note: When the screenings and particles in the integrated filter tube are enriched to a certain extent, the water flow through the integrated filter tube will decrease, and the water level in the sub-screen support containment shell will continue to rise. Each water level monitoring sensor is convenient for monitoring the water level changes in the sub-screen support containment shell, and then judging whether the integrated filter tube needs to be cleaned.

[0036] Compared with the prior art, the beneficial effects of the present invention are embodied in the following aspects:

[0037] 1. The present invention has a reasonable structural design and a fixed filter tube structure, which reduces the filter mesh surface required for conventional screen plates, reduces equipment costs, avoids wear and tear, and improves the operating stability of the equipment. The screen plates of the filter tube structure do not require sealing, which reduces the use of screen seals, reduces operating risks, and reduces equipment costs.

[0038] 2. The present invention is easy to operate and adopts a mechanical particle selection structure, which avoids the conventional screen plate screening and washing particle selection, reducing the operating cost and manufacturing and installation cost of the equipment. Especially in low temperature environments, there is no need to worry about the freezing problem of the flushing water system. At the same time, it effectively prevents the loss of anaerobic ammonia oxidation particles. The mechanical particle selection structure and the screen plate are in a vertical shearing motion, which effectively prevents the aggregation and entanglement of screen residue and particles, thereby improving the processing efficiency of the equipment.

[0039] 3. The technical solution of the present invention uses a filter array that can optimize operation based on the actual screen residue and particle enrichment, thereby achieving energy conservation, reducing wear of related filter components, and extending the service life of the equipment. It can also better adapt to the treatment requirements of low temperatures and anaerobic ammonium oxidation particles;

[0040] 4. The dynamic adjustment mechanism of the filter holes of the present invention is such that each dynamic adjustment matching hole and each integrated filtration micropore can be coaxially aligned and connected to form a filtration channel. By adjusting the overlapping area of the dynamic adjustment matching hole and the integrated filtration micropore, the cross-sectional size of the filtration channel can be adjusted to accommodate screen residues and particles of various actual particle sizes. BRIEF DESCRIPTION OF THE DRAWINGS

[0041] Figure 1 It is a front view of the present invention;

[0042] Figure 2 yes Figure 1 Right view;

[0043] Figure 3It is a schematic structural diagram of the preferred mechanism for filtering particles of the present invention;

[0044] Figure 4 It is a structural schematic diagram of the filter hole dynamic adjustment mechanism of the present invention;

[0045] Figure 5 It is a schematic structural diagram of the compressed particle discharge port of the present invention.

[0046] In the figure, 10-pretreatment flow channel, 11-screening support mechanism, 111-screening support housing, 112-screening total input pipe, 113-screening total output pipe, 20-filter tube combination mechanism, 201-fixed constraint plate, 21-filter tube combination housing, 22-comprehensive filter tube, 220-comprehensive filtration micropore, 23-filter particle optimization mechanism, 230-particle optimization drive connecting hole, 231-particle optimization shear ring shell, 232-particle optimization drive push rod, 233-drive rod linkage plate, 234-particle optimization drive support frame, 235-particle optimization drive fixed cylinder, 236-particle optimization drive sliding cylinder, 237-particle optimization drive telescopic rod, 24-filter hole dynamic adjustment mechanism, 240-dynamic adjustment matching hole, 241-filter hole adjustment matching pipe, 242-dynamic adjustment push rod, 243-dynamic adjustment fixed cylinder, 244-dynamic Adjusting sliding cylinder, 245-dynamic adjustment driving rod, 30-siphon slag discharge mechanism, 31-siphon slag discharge conveying pipe, 311-siphon slag discharge control valve, 40-particle separation mechanism, 41-particle separation holding box, 410-separation mud-water mixture discharge hole, 411-separation mud-water mixture collecting shell, 412-separation mud-water mixture output pipe, 421-compression drive holding shell, 4210-compression drive rod connecting hole, 422-particle compression push rod, 423-particle compression drive rod, 431-compressed particle discharge port, 432-particle discharge baffle, 433-particle discharge drive holding shell, 4330-discharge push rod connecting hole, 434-particle discharge push rod, 435-compressed particle discharge push plate, 436-particle discharge drive rod, 437-baffle restraining chute, 438-baffle opening and closing drive rod, 50-monitoring control mechanism, 51-water level monitoring sensor. DETAILED DESCRIPTION

[0047] The following combination Figures 1 to 5 The present invention is described in detail. For the convenience of description, the directions mentioned below are defined as follows: the up, down, left, right, front and back directions mentioned below are consistent with the up, down, left, right, front and back directions of the projection relationship of each main view or structural schematic diagram itself.

[0048] Example 1:

[0049] A rapid screening device based on low-temperature anaerobic ammonium oxidation particles, such as Figure 1 、 Figure 2As shown, it includes a screening support mechanism 11 fixed in the pretreatment flow channel 10, a filter tube assembly mechanism 20 arranged in the screening support mechanism 11, a siphon discharge mechanism 30 connected to the filter tube assembly mechanism 20, and a particle separation mechanism 40;

[0050] like Figure 1 As shown, the screening support mechanism 11 includes a screening support housing 111 fixed in the pre-treatment flow channel 10 with its opening facing upwards. A plurality of screening main inlet pipes 112 communicating with the interior of the screening support housing 111 are fixed on the upstream side thereof.

[0051] The filter tube assembly mechanism 20 includes a filter tube assembly housing 21 fixed in the screening support housing 111. A plurality of integrated filter tubes 22 with downward openings and communicating with the outside of the filter tube assembly housing 21 are fixed at the bottom of the housing.

[0052] The outer side of the filter tube assembly housing 21 is fixedly connected to the inner side wall of the sub-screening support housing 111 through a plurality of fixed constraint plates 201 extending along a vertical plane;

[0053] like Figure 3 As shown, the side wall of the integrated filter tube 22 has a plurality of integrated filter micropores 220 communicating with each other inside and outside;

[0054] A plurality of sub-screening main output pipes 113 connected to the interior of the filter tube combination housing 21 are fixed to the downstream side of the sub-screening support housing 111 .

[0055] like Figure 3 As shown, the integrated filter tube 22 is provided with a particle filtering mechanism 23, which includes a particle filtering mechanism 23 that is slidably connected to the integrated filter tube 22 and has an opening facing downward. The lower edge of the particle filtering mechanism 231 is a sharp edge structure.

[0056] The top of the integrated filter tube 22 has a vertically penetrating particle-preferred driving connection hole 230, in which a particle-preferred driving push rod 232 is slidably connected, and a particle-preferred shear ring shell 231 is fixed to the lower end of the particle-preferred driving push rod 232;

[0057] The particle-preferred driving push rod 232 extends upward to the outside of the filter tube assembly housing 21, and a horizontally arranged driving rod linkage plate 233 is fixed to the upper ends of the plurality of particle-preferred driving push rods 232;

[0058] like Figure 1As shown, a particle-preferred driving support frame 234 is fixed in the sieve support and accommodating shell 111, a particle-preferred driving fixed cylinder 235 with an opening facing downward is fixed to the bottom of the particle-preferred driving support frame 234, a particle-preferred driving sliding cylinder 236 with an opening facing upward is slidably connected in the particle-preferred driving fixed cylinder 235, and the lower end of the particle-preferred driving sliding cylinder 236 is fixedly connected to the driving rod linkage plate 233;

[0059] A particle-preferred driving telescopic rod 237 is provided in the particle-preferred driving fixed cylinder 235 for driving the particle-preferred driving sliding cylinder 236 to move up and down. The particle-preferred driving telescopic rod 237 is an electric-controlled telescopic rod driven by a servo motor in the prior art. The outer rod end of the particle-preferred driving telescopic rod 237 is fixedly connected to the top of the particle-preferred driving fixed cylinder 235, and the inner rod end of the particle-preferred driving telescopic rod 237 is fixedly connected to the bottom of the particle-preferred driving sliding cylinder 236.

[0060] like Figure 2 As shown, the siphon slag discharge mechanism 30 includes a siphon slag discharge conveying pipe 31 fixed to the bottom of the screening support and accommodating shell 111 and connected to the interior thereof.

[0061] like Figure 1 As shown, a monitoring and control mechanism 50 is provided on the inner wall of the screening support and containing shell 111. The monitoring and control mechanism 50 includes a plurality of water level monitoring sensors 51 fixed on the inner wall of the screening support and containing shell 111. The plurality of water level monitoring sensors 51 are evenly dispersed along the vertical direction on the inner wall of the screening support and containing shell 111.

[0062] The water level monitoring sensor 51 is a commercially available water level sensor in the prior art.

[0063] Example 2:

[0064] On the basis of Example 1, Figure 3 As shown, the integrated filter tube 22 is provided with a filter hole dynamic adjustment mechanism 24, which includes a filter hole adjustment matching tube 241 slidably connected to the outside of the integrated filter tube 22, and a plurality of dynamic adjustment matching holes 240 extending radially through the side wall of the filter hole adjustment matching tube 241;

[0065] The aperture and relative position of the dynamic adjustment matching hole 240 and the integrated filtering micropore 220 are consistent;

[0066] like Figure 4 As shown, a vertically extending dynamic adjustment push rod 242 is fixed to the filter hole adjustment matching tube 241, and a downwardly opening dynamic adjustment fixed cylinder 243 is fixed to the outer side of the integrated filter tube 22 near the top. A upwardly opening dynamic adjustment sliding cylinder 244 is slidably connected to the dynamic adjustment fixed cylinder 243, and the lower end of the dynamic adjustment sliding cylinder 244 is fixedly connected to the dynamic adjustment push rod 242;

[0067] A dynamic adjustment driving rod 245 is provided in the dynamic adjustment fixed cylinder 243 for driving the dynamic adjustment sliding cylinder 244 to move up and down. The dynamic adjustment driving rod 245 is an electrically controlled telescopic rod driven by a servo motor in the prior art. The outer rod end of the dynamic adjustment driving rod 245 is fixedly connected to the top inner side of the dynamic adjustment fixed cylinder 243, and the inner rod end of the dynamic adjustment driving rod 245 is fixedly connected to the bottom inner side of the dynamic adjustment sliding cylinder 244.

[0068] Example 3:

[0069] On the basis of Example 2, Figure 2 As shown, the particle separation mechanism 40 includes a particle separation container 41 fixed to the end of the siphon discharge conveying pipe 31 away from the screening support container 111. The particle separation container 41 is a horizontally extending box structure, and a particle separation extrusion slider 42 is slidably fitted in the particle separation container 41.

[0070] A separation mud-water mixture collecting shell 411 is fixed to the bottom of the particle separation holding box 41. A plurality of separation mud-water mixture discharge holes 410 are provided on the lower side of the particle separation holding box 41, which are connected to the interior of the separation mud-water mixture collecting shell 411. A separation mud-water mixture output pipe 412 is fixed to the bottom of the separation mud-water mixture collecting shell 411, which is connected to the interior of the separation mud-water mixture collecting shell 411.

[0071] A compression drive housing 421 is fixed to the end of the particle separation housing box 41. The end of the particle separation housing box 41 has a compression drive rod connection hole 4210 that runs horizontally through the end of the particle separation housing box 41 and is connected to the interior of the compression drive housing 421. A particle compression push rod 422 is slidably connected to the compression drive rod connection hole 4210. One end of the particle compression push rod 422 located inside the particle separation housing box 41 is fixedly connected to the particle separation extrusion slider 42.

[0072] A particle compression drive rod 423 is provided in the compression drive housing 421 for driving the particle compression push rod 422 to move. The particle compression drive rod 423 is an electrically controlled telescopic rod driven by a servo motor in the prior art. The outer rod end of the particle compression drive rod 423 is fixedly connected to the compression drive housing 421, and the inner rod end of the particle compression drive rod 423 is fixedly connected to the particle compression push rod 422.

[0073] The siphon slag conveying pipe 31 has a siphon slag control valve 311 at one end close to the screening support housing 111 and at one end close to the particle separation housing 41. The siphon slag control valve 311 is a butterfly valve in the prior art.

[0074] like Figure 2 As shown, the lower side of the particle separation holding box 41 away from the particle separation extrusion slider 42 has a compressed particle discharge port 431 that communicates with the inside and outside. Figure 5 As shown, a particle discharge baffle 432 is slidably connected to the compressed particle discharge port 431 on the lower side of the particle separation and holding box 41;

[0075] like Figure 5 As shown, a particle discharge driving accommodating shell 433 is fixed on the upper side of the particle separation accommodating box 41 and above the compressed particle discharge port 431. The upper side of the particle separation accommodating box 41 has an discharge push rod connecting hole 4330 that vertically passes through and is connected to the interior of the particle discharge driving accommodating shell 433. A particle discharge push rod 434 is slidably connected in the discharge push rod connecting hole 4330. A compressed particle discharge push plate 435 is fixed at one end of the particle discharge push rod 434 in the particle separation accommodating box 41. A particle discharge driving rod 436 for driving the particle discharge pushing rod 434 to move is provided in the particle discharge driving accommodating shell 433. The particle discharge driving rod 436 is an electrically controlled telescopic rod driven by a servo motor in the prior art. The outer rod end of the particle discharge driving rod 436 is fixedly connected to the top of the particle discharge driving accommodating shell 433, and the inner rod end of the particle discharge driving rod 436 is fixedly connected to the upper end of the particle discharge pushing rod 434.

[0076] A horizontally extending baffle constraint slot 437 is fixed to the lower side of the particle separation holding box 41, and the particle discharge baffle 432 slides in the baffle constraint slot 437. A baffle opening and closing drive rod 438 for driving the particle discharge baffle 432 to move is fixed to the end of the particle separation holding box 41. The baffle opening and closing drive rod 438 is an electrically controlled telescopic rod driven by a servo motor in the prior art. The outer rod end of the baffle opening and closing drive rod 438 is fixedly connected to the particle separation holding box 41, and the inner rod end of the baffle opening and closing drive rod 438 is fixedly connected to the particle discharge baffle 432.

[0077] In the actual application process of the present invention, Figure 1 As shown, the mud-water mixture in the pre-treatment flow channel 10 flows from left to right, the left side of the sub-screen support housing 111 is called the upstream end, and the right side of the sub-screen support housing 111 is called the downstream end;

[0078] During the circulation of the mud-water mixture in the pretreatment circulation channel 10, it enters the interior of the sub-screening support and containing shell 111 through multiple sub-screening main input pipes 112, and the mud-water mixture is collected in the sub-screening support and containing shell 111 and the water level is gradually raised. During the water level rising process in the sub-screening support and containing shell 111, the mud-water mixture enters the interior of the comprehensive filter tube 22 through the lower end of the comprehensive filter tube 22, and the mud-water mixture entering the interior of the comprehensive filter tube 22 flows from the inside to the outside through the comprehensive filter micropores 220, thereby filtering the mud-water mixture, and the screening residue and particles in the mud-water mixture will be intercepted and retained in the interior of the comprehensive filter tube 22, and the filtered mud-water mixture enters the interior of the filter tube combination containing shell 21, and the filtered mud-water mixture in the filter tube combination containing shell 21 is discharged to the downstream end of the sub-screening support and containing shell 111 through the sub-screening main output pipe 113, and the filtered mud-water mixture continues to circulate in the pretreatment circulation channel 10 and enters the subsequent mud-water mixture treatment process;

[0079] The water level monitoring sensors 51 are numbered from bottom to top as S1, S2, S3, S4, and S5. Assuming that the integrated filter tube 22 is operating in normal filtration processing, the water level balance in the sub-screening support housing 111 is between S3 and S4. When the screening residue and particles in the integrated filter tube 22 are enriched to a certain extent, the water flow through the integrated filter tube 22 will decrease, and the water level in the sub-screening support housing 111 will continue to rise until the water level monitoring sensor 51 numbered S4 detects a water level signal, indicating that the integrated filter tube 22 needs to be cleaned.

[0080] When the screenings and particles accumulated inside the integrated filter tube 22 cause the filtering performance of the integrated filter tube 22 to decrease, the screenings and particles intercepted inside the integrated filter tube 22 are cleaned by the filter particle selection mechanism 23;

[0081] The inner rod of the particle-preferred driving telescopic rod 237 extends to drive the particle-preferred driving sliding cylinder 236, the driving rod linkage plate 233 and the plurality of particle-preferred driving push rods 232 to move downward in the vertical direction. The plurality of particle-preferred driving push rods 232 then drive the particle-preferred shearing ring shells 231 to move from top to bottom in the integrated filter tube 22. The edge structure of the lower end edge of the particle-preferred shearing ring shell 231 is used to shovel off the screening residue and particles attached to the inner wall of the integrated filter tube 22, and under the push of the particle-preferred shearing ring shell 231, the screening residue and particles are pushed out from the lower end of the integrated filter tube 22.

[0082] Then the particle-preferred driving inner rod of the telescopic rod 237 is retracted, so that the particle-preferred shear ring shell 231 is returned to the top of the integrated filter tube 22;

[0083] The screenings and particles cleaned out from the integrated filter tube 22 will accumulate at the bottom of the screening support housing 111;

[0084] The siphon discharge mechanism 30 is used to discharge the screenings and particles accumulated at the bottom of the screening support and accommodating shell 111, and the particle separation mechanism 40 is used to compress and dehydrate the screenings and particles;

[0085] Simultaneously, the siphon discharge control valves 311 at both ends of the siphon discharge conveying pipe 31 are opened. Under the action of gravity, the mud-water mixture mixed with the screenings and particles will pass through the siphon discharge conveying pipe 31 into the particle separation holding box 41. After the particle separation holding box 41 is filled, the siphon discharge control valves 311 at both ends of the siphon discharge conveying pipe 31 are simultaneously closed.

[0086] In the initial state, the particle separation and extrusion slider 42 is located inside the particle separation holding box 41 at a side away from the siphon discharge conveying pipe 31. After the particle separation holding box 41 is filled with screenings and particles, the inner rod of the particle compression driving rod 423 extends and drives the particle separation and extrusion slider 42 to move inside the particle separation holding box 41 through the particle discharge push rod 434, thereby squeezing the screenings and particles. The moisture in the screenings and particles will be squeezed out and enter the separation mud and water mixture collection shell 411 through the separation mud and water mixture discharge hole 410. The mud and water mixture in the separation mud and water mixture collection shell 411 can finally be discharged from the separation mud and water mixture output pipe 412.

[0087] In the initial state, the particle discharge baffle 432 blocks the lower side of the compressed particle discharge port 431, so that the compressed particle discharge port 431 is in a closed state, and the compressed particle push plate 435 is at the top position in the particle separation and holding box 41;

[0088] After the screen residue and particles are compressed, they are located at the compressed particle discharge port 431. The inner rod of the baffle opening and closing driving rod 438 extends to drive the particle discharge baffle 432 away from the compressed particle discharge port 431, so that the compressed particle discharge port 431 is in an open state.

[0089] Then the inner rod of the particle discharge driving rod 436 extends to drive the particle discharge push rod 434 and the compressed particle discharge push plate 435 to move from top to bottom. Under the push of the compressed particle discharge push plate 435, the compressed screen residue and particles are pushed out from the compressed particle discharge port 431.

[0090] Between each filter hole adjustment fitting tube 241 and the integrated filter tube 22, each dynamic adjustment fitting hole 240 and each integrated filter micropore 220 can be coaxially aligned and connected at the same time. When the dynamic adjustment fitting hole 240 and the integrated filter micropore 220 are connected, a filter channel is formed together. By adjusting the overlapping area of the dynamic adjustment fitting hole 240 and the integrated filter micropore 220, the cross-sectional size of the filter channel can be adjusted to accommodate screen residues and particles of various actual particle sizes.

[0091] The extension or retraction of the inner rod of the dynamic adjustment driving rod 245 can drive the dynamic adjustment sliding cylinder 244, the dynamic adjustment push rod 242 and the filter hole adjustment matching tube 241 to move in the vertical direction, thereby controlling the overlapping area between each dynamic adjustment matching hole 240 and each integrated filtration micropore 220.

Claims

1. A rapid screening device based on low-temperature anaerobic ammonium oxidation particles, characterized in that: It comprises a screening support mechanism (11) fixed in a pretreatment flow channel (10), a filter tube assembly mechanism (20) arranged in the screening support mechanism (11), a siphon discharge mechanism (30) connected to the filter tube assembly mechanism (20), and a particle separation mechanism (40); The sub-screening support mechanism (11) comprises a sub-screening support housing (111) fixed in the pre-treatment flow channel (10) and with its opening facing upwards, and a plurality of sub-screening main inlet pipes (112) connected to the interior of the sub-screening support housing (111) are fixed on the upstream side of the sub-screening support housing (111); The filter tube assembly mechanism (20) comprises a filter tube assembly housing (21) fixed in the sub-screening support housing (111), wherein a plurality of integrated filter tubes (22) with downward openings and communicating with the outside of the filter tube assembly housing (21) are fixed to the bottom of the housing; The side wall of the integrated filtering tube (22) is provided with a plurality of integrated filtering micropores (220) communicating with each other inside and outside; A plurality of sub-screening total output pipes (113) connected to the interior of the filter tube combination housing (21) are fixed on the downstream side of the sub-screening support housing (111).

2. A rapid screening device based on low-temperature anaerobic ammonium oxidation particles according to claim 1, characterized in that: The integrated filter tube (22) is provided with a particle filtering mechanism (23), the particle filtering mechanism (23) comprising a particle preferred shearing ring shell (231) slidably connected to the integrated filter tube (22) and with an opening facing downward, the lower end edge of the particle preferred shearing ring shell (231) being a sharp edge structure; The top end of the integrated filter tube (22) is provided with a vertically penetrating particle-preferred driving connection hole (230), a particle-preferred driving push rod (232) is slidably connected in the particle-preferred driving connection hole (230), and the particle-preferred shear ring shell (231) is fixed to the lower end of the particle-preferred driving push rod (232); The particle-preferred driving push rod (232) extends upward to the outside of the filter tube assembly housing (21), and a horizontally arranged driving rod linkage plate (233) is commonly fixed to the upper ends of a plurality of the particle-preferred driving push rods (232); A particle-preferred driving support frame (234) is fixed in the sieve support and accommodating shell (111), a particle-preferred driving fixed cylinder (235) with an opening facing downward is fixed to the bottom of the particle-preferred driving support frame (234), a particle-preferred driving sliding cylinder (236) with an opening facing upward is slidably connected in the particle-preferred driving fixed cylinder (235), and the lower end of the particle-preferred driving sliding cylinder (236) is fixedly connected to the driving rod linkage plate (233); The particle-preferred driving fixed cylinder (235) is provided with a particle-preferred driving telescopic rod (237) for driving the particle-preferred driving sliding cylinder (236) to move up and down.

3. A rapid screening device based on low-temperature anaerobic ammonium oxidation particles according to claim 1, characterized in that: The integrated filter tube (22) is provided with a filter hole dynamic adjustment mechanism (24), the filter hole dynamic adjustment mechanism (24) comprising a filter hole adjustment matching tube (241) slidably connected to the outside of the integrated filter tube (22), and a plurality of dynamic adjustment matching holes (240) penetrating along the radial direction of the filter hole adjustment matching tube (241) are provided on the side wall thereof; The aperture and relative position of the dynamic adjustment matching hole (240) and the integrated filtering micropore (220) are consistent; A vertically extending dynamic adjustment push rod (242) is fixed on the filter hole adjustment matching tube (241); a downwardly opening dynamic adjustment fixed cylinder (243) is fixed near the top of the outer side of the integrated filter tube (22); a upwardly opening dynamic adjustment sliding cylinder (244) is slidably connected inside the dynamic adjustment fixed cylinder (243); the lower end of the dynamic adjustment sliding cylinder (244) is fixedly connected to the dynamic adjustment push rod (242); The dynamic adjustment fixed cylinder (243) is provided with a dynamic adjustment driving rod (245) for driving the dynamic adjustment sliding cylinder (244) to move upward and downward.

4. The rapid screening equipment based on low-temperature anaerobic ammonium oxidation particles according to claim 1, characterized in that: The siphon slag discharge mechanism (30) comprises a siphon slag discharge conveying pipe (31) fixed to the bottom of the screening support and accommodating shell (111) and connected to the interior thereof.

5. A rapid screening device based on low-temperature anaerobic ammonium oxidation particles according to claim 4, characterized in that: The particle separation mechanism (40) comprises a particle separation accommodating box (41) fixed to one end of the siphon slag discharge conveying pipe (31) away from the screening support accommodating shell (111); the particle separation accommodating box (41) is a horizontally extending box structure; a particle separation extrusion slider (42) is slidably fitted in the particle separation accommodating box (41); A separation mud-water mixture collecting shell (411) is fixed at the bottom of the particle separation holding box (41); a plurality of separation mud-water mixture discharge holes (410) are provided on the lower side of the particle separation holding box (41) and are communicated with the interior of the separation mud-water mixture collecting shell (411); a separation mud-water mixture output pipe (412) is fixed at the bottom of the separation mud-water mixture collecting shell (411) and is communicated with the interior thereof; A compression drive housing (421) is fixed to the end of the particle separation housing box (41), and the end of the particle separation housing box (41) has a compression drive rod connecting hole (4210) that runs horizontally through and is connected to the interior of the compression drive housing (421). A particle compression push rod (422) is slidably connected to the compression drive rod connecting hole (4210), and one end of the particle compression push rod (422) located in the particle separation housing box (41) is fixedly connected to the particle separation extrusion slider (42); A particle compression driving rod (423) for driving the particle compression push rod (422) to move is provided in the compression driving accommodating shell (421); The siphon slag discharge conveying pipe (31) is provided with a siphon slag discharge control valve (311) at one end close to the screening support housing (111) and at one end close to the particle separation housing box (41).

6. A rapid screening device based on low-temperature anaerobic ammonium oxidation particles according to claim 5, characterized in that: The particle separation holding box (41) has a compressed particle discharge port (431) communicating with the inside and outside of the particle separation holding box (41) at its lower side away from one end of the particle separation extrusion slider (42), and a particle discharge baffle (432) is slidably connected to the compressed particle discharge port (431) at the lower side of the particle separation holding box (41); A particle discharge drive housing (433) is fixed on the upper side of the particle separation housing box (41) and above the compressed particle discharge port (431). The upper side of the particle separation housing box (41) has a discharge push rod connecting hole (4330) that is vertically through and connected to the interior of the particle discharge drive housing box (433). A particle discharge push rod (434) is slidably connected in the discharge push rod connecting hole (4330). A compressed particle discharge push plate (435) is fixed to one end of the particle discharge push rod (434) in the particle separation housing box (41). A particle discharge drive housing (433) is provided with a particle discharge drive rod (436) for driving the particle discharge push rod (434) to move.

7. The rapid screening equipment based on low-temperature anaerobic ammonium oxidation particles according to claim 1, characterized in that: A monitoring and control mechanism (50) is provided on the inner side wall of the sub-screening support and accommodating shell (111). The monitoring and control mechanism (50) comprises a plurality of water level monitoring sensors (51) fixed on the inner side wall of the sub-screening support and accommodating shell (111). The plurality of water level monitoring sensors (51) are evenly dispersed and arranged in a vertical direction on the inner side wall of the sub-screening support and accommodating shell (111).