Integrally assembled biochemical device capable of reducing biochemical energy consumption
By adopting a modular main tank and baffles to form a five-stage AO process in the sewage treatment device, combined with an internal reflux rotary gate, and optimizing the structure of the biological treatment tank, the problems of high energy consumption and long construction period are solved, achieving the effects of low energy consumption, convenient construction and efficient operation and maintenance.
Patent Information
- Application Number
- CN202423253332.9
- Authority / Receiving Office
- CN · China
- Patent Type
- Utility models(China)
- Current Assignee / Owner
- Filing Date
- 2024-12-28
- Publication Date
- 2026-01-02
- Estimated Expiration
- 2034-12-28
AI Technical Summary
Existing integrated sewage treatment devices suffer from high energy consumption and unreasonable tank structure, resulting in long construction cycles, high operation and maintenance costs, and poor convenience for recycling and reuse.
An integrated modular biochemical device is constructed by using a modular main tank and multiple modular partitions to form a modular structure. It has a five-stage AO process and achieves water reflux through an internal reflux rotary gate, eliminating the need for a nitrification liquid reflux pump and optimizing the internal structure of the biochemical tank.
It reduces biochemical energy consumption, shortens the construction cycle, saves transportation costs and construction time, reduces operation and maintenance costs, and improves the convenience of recycling and reuse.
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Figure CN223752575U_ABST
Abstract
Description
TECHNICAL FIELD
[0001] The utility model relates to the field of sewage treatment and resource technology, especially to a biochemical device of integrated assembly reducing biochemical energy consumption. BACKGROUND
[0002] Biochemical pond energy consumption is an important issue in the field of sewage treatment, which directly relates to the operation cost of sewage treatment plant, energy utilization efficiency and environmental protection effect. High biochemical pond energy consumption not only increases the cost of sewage treatment, but also may have negative impact on the environment and economy. The specific performance is as follows:
[0003] Cost increase: high energy consumption leads to the increase of sewage treatment cost, which brings economic pressure to the sewage treatment plant.
[0004] Resource waste: unnecessary energy consumption wastes valuable energy resources, which is contrary to the concept of sustainable development.
[0005] Environmental pollution: if fossil energy is used as power source, high energy consumption will increase carbon emissions and aggravate environmental pollution problems.
[0006] In a sewage treatment plant using biochemical process, the biochemical pond as the main monomer is self-evident. With the progress of technology and the improvement of environmental protection requirements, more and more sewage treatment plants begin to use integrated device instead of traditional civil structure biochemical pond. This change not only improves the construction efficiency, but also optimizes the sewage treatment process and reduces the operation cost. Although the existing integrated device has the advantages of short construction period, small land occupation, low operation cost and convenient maintenance, etc., but there are problems of high energy consumption caused by unreasonable structure in the pond body and poor convenience of recycling and reuse of the pond body.
[0007] Therefore, the utility model is proposed. CONTENT OF THE UTILITY MODEL
[0008] The utility model aims at providing an integrated assembly biochemical device of reducing biochemical energy consumption, which is convenient to disassemble and assemble, shortens the construction period, is convenient for recycling and reuse, has reasonable internal structure, can reduce the operation energy consumption, and solves the above technical problems in the prior art.
[0009] The utility model aims at realizing the following technical scheme:
[0010] An integrated assembly biochemical device of reducing biochemical energy consumption, characterized by comprising:
[0011] The assembly type total pond body, a plurality of assembly type baffles, a water inlet pipe, an anaerobic pond, a primary anoxic pond, a primary aerobic pond, a secondary anoxic pond, a secondary aerobic pond, a water outlet pipe, a plurality of submersible flow inducers and two internal reflux rotary gates, wherein,
[0012] The plurality of assembled partition plates are arranged in the assembled total pool body, and the assembled total pool body is divided into an anaerobic pool, a first anoxic pool, a first aerobic pool, a second anoxic pool and a second aerobic pool which are sequentially communicated, and the communicated anaerobic pool, first anoxic pool, first aerobic pool, second anoxic pool and second aerobic pool form a five-stage AO process of an outer ring plus an inner return flow channel in the assembled total pool body;
[0013] The front end of the anaerobic pool is connected with an inlet pipe;
[0014] The rear end of the second aerobic pool is connected with an outlet pipe;
[0015] Two submerged flow promoters are arranged in the first anoxic pool;
[0016] One submerged flow promoter is arranged in the second anoxic pool;
[0017] The end of the first aerobic pool is communicated with the first anoxic pool through one inner return flow rotary gate arranged on the assembled partition plate;
[0018] The end of the first aerobic pool is communicated with the second anoxic pool through another inner return flow rotary gate arranged on the assembled partition plate.
[0019] Compared with the prior art, the integrated assembled biochemical device for reducing biochemical energy consumption has the beneficial effects including:
[0020] The integrated assembled biochemical device with an overall assembled structure is formed by adopting the assembled total pool body and the plurality of assembled partition plates, can be assembled on site, saves freight and construction time, and due to the sequential communication of the anaerobic pool, first anoxic pool, first aerobic pool, second anoxic pool and second aerobic pool, the communicated anaerobic pool, first anoxic pool, first aerobic pool, second anoxic pool and second aerobic pool form a five-stage AO process of an outer ring plus an inner return flow channel in the assembled total pool body, and the inner return flow rotary gate is adopted to return flow from the first aerobic pool to the first and second anoxic pools, so that the nitrification liquid return flow pump is cancelled, and the operation and maintenance cost is saved. BRIEF DESCRIPTION OF DRAWINGS
[0021] In order to more clearly illustrate the technical scheme of the embodiments of the present application, the following will briefly introduce the drawings needed to be used in the embodiment description. Obviously, the drawings in the following description are only some embodiments of the present application, and other drawings can also be obtained by those skilled in the art without creative labor.
[0022] Figure 1 The structure diagram of the integrated assembled biochemical device for reducing biochemical energy consumption provided by the embodiments of the present application.
[0023] Corresponding components of the various marks in the drawings are identified by the same reference numerals. 1 - water inlet pipe, 2 - anaerobic tank, 3 - first stage anoxic tank, 4 - first stage aerobic tank, 5 - second stage anoxic tank, 6 - second stage aerobic tank, 7 - water outlet pipe, 8 - submersible flow inducer, 9 - internal reflux rotary gate, 10 - integrated equipment foundation, 11 - assembled partition; 12 - assembled total tank body. DETAILED DESCRIPTION
[0024] The technical solutions in the embodiments of the present application will be clearly and completely described below with reference to the drawings in the embodiments of the present application. Obviously, the described embodiments are only part of the embodiments of the present application, rather than all the embodiments of the present application, which do not constitute a limitation on the present application. Based on the embodiments of the present application, all other embodiments obtained by those skilled in the art without creative labor fall within the protection scope of the present application.
[0025] First, the terms possibly used in the present text are described as follows:
[0026] The term "and / or" means either one or both, for example, X and / or Y means three cases including "X", "Y" or "X and Y".
[0027] The terms "include", "contain", "have", "possess" or other similar semantic descriptions should be interpreted as non-exclusive inclusion. For example, including a technical feature element (such as raw materials, components, ingredients, carriers, dosage forms, materials, sizes, parts, components, mechanisms, devices, steps, processes, methods, reaction conditions, processing conditions, parameters, algorithms, signals, data, products or articles, etc.) should be interpreted as not only including the explicitly listed technical feature element, but also including other technical feature elements not explicitly listed in the art.
[0028] The term "consisting of" means excluding any technical feature element not explicitly listed. If this term is used in the claims, the term will make the claim closed, so that it does not contain technical feature elements other than the explicitly listed technical feature elements, except for conventional impurities related thereto. If the term only appears in a certain clause of the claim, it is only limited to the elements explicitly listed in that clause, and the elements described in other clauses are not excluded from the overall claim.
[0029] Unless otherwise defined, the terms "mounting", "connected", "connection", "fixed", and the like are to be construed in a broad sense, for example: can be fixed connection, can also be detachable connection, or integrally connected; can be mechanical connection, can also be electrical connection; can be directly connected, can also be indirectly connected through an intermediate medium, can be internal communication of two elements. For those skilled in the art, the specific meaning of the above terms in this paper can be understood according to the specific circumstances.
[0030] The orientation or positional relationship indicated by the terms "center", "longitudinal", "transverse", "length", "width", "thickness", "upper", "lower", "front", "rear", "left", "right", "vertical", "horizontal", "top", "bottom", "inner", "outer", "clockwise", "counterclockwise", etc. is based on the orientation or positional relationship shown in the drawings, and is only for the convenience of description and simplification of description, and does not mean or imply that the device or element referred to must have a particular orientation, be constructed and operated in a particular orientation, and therefore cannot be understood as limiting this paper.
[0031] The scheme provided by the utility model will be described in detail below. The contents not described in detail in the embodiments of the utility model belong to the prior art known to those skilled in the art. If no specific conditions are specified in the embodiments of the utility model, the conditions are in accordance with the conventional conditions in the art or the conditions recommended by the manufacturer. If no manufacturer of the reagent or instrument used in the embodiments of the utility model is specified, it is a conventional product that can be obtained by market purchase.
[0032] As shown in Figure 1 The utility model discloses a kind of integrated assembly biochemical devices for reducing biochemical energy consumption, comprising:
[0033] Assembling type total pool body 12, multiple assembling type partition plates 11, water inlet pipe 1, anaerobic tank 2, first anoxic tank 3, first aerobic tank 4, second anoxic tank 5, second aerobic tank 6, water outlet pipe 7, multiple submersible flow inducers 8 and two internal reflux rotary gates 9;Wherein,
[0034] The assembling type total pool body 12 is provided with multiple assembling type partition plates 11, and the assembling type total pool body 12 is divided into anaerobic tank 2, first anoxic tank 3, first aerobic tank 4, second anoxic tank 5 and second aerobic tank 6 in sequence, and the anaerobic tank 2, first anoxic tank 3, first aerobic tank 4, second anoxic tank 5 and second aerobic tank 6 after being communicated form five-stage AO process of outer ring plus inner turn-back water flow channel in the assembling type total pool body 12;
[0035] The front end of anaerobic tank 2 is connected with water inlet pipe 1;
[0036] The rear end of second aerobic tank 6 is connected with water outlet pipe 2;
[0037] The primary anoxic tank 3 is provided with two submersible flow promoters 8;
[0038] The secondary anoxic tank 5 is provided with one submersible flow promoter 8;
[0039] The end of the primary aerobic tank 4 is communicated with the primary anoxic tank 3 through one internal reflux rotary gate 9 arranged on the assembled partition 11;
[0040] The end of the primary aerobic tank 4 is communicated with the secondary anoxic tank 5 through another internal reflux rotary gate 9 arranged on the assembled partition 11.
[0041] Preferably, in the above device, the assembled total tank body 12 is a tank body with a cuboid structure assembled from a plurality of enamel steel plates on the basis of an integrated device. The total tank body with such a structure is convenient to install, can shorten the construction period, is good in subsequent recovery convenience, and has the advantages of high hardness, strong weather resistance, corrosion resistance, and simple installation, etc.
[0042] Preferably, in the above device, the plurality of assembled partitions 11 all adopt enamel steel plates. Also has the advantages of high hardness, strong weather resistance, corrosion resistance, and simple installation, etc.
[0043] Preferably, in the above device, in the assembled total tank body 12, the anaerobic tank 2 is located at a corner of the front end of the assembled total tank body 12, a one-section tank body and a two-section tank body of the primary anoxic tank 3 are arranged in sequence along the side of the anaerobic tank 2, the two-section tank body is located at the inside and outside of the assembled total tank body 12 and occupies the front-to-back position of the inside and outside of the assembled total tank body 12, the primary aerobic tank 4 is arranged on the inside of the primary anoxic tank 3, the primary aerobic tank 4 is composed of three-section tank bodies arranged in sequence and communicated, the secondary anoxic tank 5 and the secondary aerobic tank 6 are arranged in parallel on the inside of the primary aerobic tank 4, and the secondary aerobic tank 6 is located at a corner of the rear end of the same side of the assembled total tank body 12 as the anaerobic tank 2;
[0044] The one-section tank body and the two-section tank body of the primary anoxic tank 3 form an outer annular water flow channel with the anaerobic tank 2, and the three-section tank bodies of the primary aerobic tank 4, the secondary anoxic tank 5, and the secondary aerobic tank 6 form a turning-back water flow channel.
[0045] Preferably, in the above device, the primary anoxic tank 3 is provided with two submersible flow promoters 8.
[0046] One submersible flow promoter 8 is arranged at the side end of the one-section tank body of the primary anoxic tank 3, and another submersible flow promoter 8 is arranged at the front end of the two-section tank body.
[0047] Preferably, in the above device, one submersible flow promoter 8 is arranged at the front end of the secondary anoxic tank 5.
[0048] Preferably, in the device, the end of the first aerobic tank 4 is communicated with the beginning of the first anoxic tank 3 through an inner reflux rotary gate 9 arranged on the assembled partition plate 11.
[0049] Preferably, in the device, the end of the first aerobic tank 4 is communicated with the beginning of the second anoxic tank 5 through another inner reflux rotary gate 9 arranged on the assembled partition plate 11.
[0050] As can be seen from the above, the integrated assembled biochemical device of the embodiment of the present application is of an assembled structure as a whole, can be assembled on site, saves freight and construction time, and forms a five-stage AO process of an outer ring plus an inner return flow channel in the assembled total tank body, and uses an inner reflux rotary gate to reflux from the first aerobic tank to the first and second anoxic tanks, cancels the nitrification liquid reflux pump, and saves operation and maintenance cost.
[0051] In order to more clearly show the technical scheme provided by the present application and the technical effects generated, the scheme provided by the embodiment of the present application is described in detail below with specific examples.
[0052] Embodiment 1
[0053] The embodiment of the present application provides an integrated assembled biochemical device for reducing biochemical energy consumption, which can be used for sewage biochemical treatment, such as Figure 1 As shown in the figure, the integrated assembled biochemical device comprises:
[0054] The assembled total pool body 12, the plurality of assembled partition plates 11, the water inlet pipe 1, the anaerobic pool 2, the first-stage anoxic pool 3, the first-stage aerobic pool 4, the second-stage anoxic pool 5, the second-stage aerobic pool 6, the water outlet pipe 7, the plurality of submersible push-flow devices 8 and the two internal reflux rotary gates 9; wherein the assembled total pool body 12 is divided by the plurality of assembled partition plates 11 to form the anaerobic pool 2, the first-stage anoxic pool 3, the first-stage aerobic pool 4, the second-stage anoxic pool 5 and the second-stage aerobic pool 6 in turn, and constitutes a five-stage AO process, and the mixed flora in the five-stage AO process alternately is in anoxic and aerobic states, which is beneficial to improve the sludge settling performance and reduce the occurrence of sludge bulking. Meanwhile, the second-stage aerobic improves the dissolved oxygen content of the sewage, can reduce the sludge phosphorus release amount of the secondary sedimentation tank, and is suitable for treating projects with large water quantity and quality fluctuations or high total nitrogen and total phosphorus values of the inlet water; the submersible push-flow devices 8 are arranged in the first-stage anoxic pool 3 and the second-stage anoxic pool 5 respectively, so that the water flow in the anoxic section forms a push-flow state; the internal reflux rotary gates 9 are separately arranged at the end of the first-stage aerobic pool 4 and the beginning of the first-stage anoxic pool 3 and the second-stage anoxic pool 5; by optimizing the internal structure of the biochemical pool, the internal reflux is performed by the submersible push-flow devices 8 in cooperation with the internal reflux rotary gates 9, the water flow mixing efficiency and mass transfer effect are improved, the internal reflux pump does not need to be additionally arranged, and the energy consumption and equipment maintenance are reduced. Meanwhile, the reflux water amount can be adjusted by adjusting the rotation speed of the submersible push-flow device 8 and the opening angle of the internal reflux rotary gate 9; the integrated assembled biochemical device is arranged regularly, does not need to be transported integrally, is on-site spliced by enamel steel plates, and the equipment transportation cost is reduced; when the device is used as a temporary sewage treatment facility, the enamel steel plates 11 used for assembly have the characteristics of high hardness, strong weather resistance, corrosion resistance, simple installation and the like, can be relocated and recycled.
[0055] As can be seen from the above, the integrated assembled biochemical device uses enamel steel plates as the assembly material, can be on-site assembled, saves transportation cost and construction time, cancels the nitrification liquid reflux pump, uses the internal reflux gate for reflux, and saves operation and maintenance cost.
[0056] The above merely describes a preferred specific embodiment of the present application, but the protection scope of the present application is not limited to this. Any skilled person in the art can easily think of changes or replacements within the technical range disclosed by the present application, which should be covered in the protection scope of the present application. Therefore, the protection scope of the present application should be subject to the protection scope of the claims. The information disclosed in the background art part of the present application is merely intended to deepen the understanding of the overall background art of the present application, and should not be regarded as acknowledging or implying in any form that the information constitutes the prior art known by the skilled person.
Claims
1. An integrated assembly of biochemicals for reducing biochemical energy consumption, characterized in that, The application relates to a five-stage AO process device. The application relates to a five-stage AO process device. The application relates to a five-stage AO process device. The application relates to a five-stage AO process device. The application relates to a five-stage AO process device. The application relates to a five-stage AO process device. The application relates to a five-stage AO process device. The application relates to a five-stage AO process device. The application relates to a five-stage AO process device.
2. The integrated assembled biochemical device for reducing biochemical energy consumption according to claim 1, wherein, The application relates to a five-stage AO process device.
3. The integrated assembled biochemical device for reducing biochemical energy consumption according to claim 1, wherein, The application relates to a five-stage AO process device.
4. The integrated assembled biochemical device for reducing biochemical energy consumption according to any one of claims 1-3, characterized in that, The application relates to a five-stage AO process device. The application relates to a five-stage AO process device.
5. The integrated assembled biochemical device for reducing biochemical energy consumption according to claim 4, wherein, The application relates to a five-stage AO process device. The application relates to a five-stage AO process device.
6. The integrated assembled biochemical device for reducing biochemical energy consumption according to claim 4, wherein, The application relates to a five-stage AO process device. The application relates to a five-stage AO process device. The application relates to a five-stage AO process device. The application relates to a five-stage AO process device. The application relates to a five-stage AO process device. The application relates to a five-stage AO process device. The application relates to a five-stage AO process device. The application relates to a five-stage AO process device. The application relates to a five-stage AO process device. The application relates to a five-stage AO process device. The application relates to a five-stage AO process device. The application relates to a five-stage AO process device. The application relates to a five-stage AO process device. The application relates to a five-stage AO process device. 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The integrated assembled biochemical device for reducing biochemical energy consumption according to any one of claims 1-3, wherein, The end of the primary aerobic tank (4) is communicated with the inner end of the primary anoxic tank (3) through an inner reflux rotary gate (9) arranged on the assembled partition (11).
8. The integrated assembled biochemical device for reducing biochemical energy consumption according to any one of claims 1-3, wherein, The end of the primary aerobic tank (4) is communicated with the inner end of the secondary anoxic tank (5) through another inner reflux rotary gate (9) arranged on the assembled partition (11).