CN114524516B - Biochemical reactor and sewage treatment method - Google Patents
Biochemical reactor and sewage treatment method Download PDFInfo
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- CN114524516B CN114524516B CN202210187138.1A CN202210187138A CN114524516B CN 114524516 B CN114524516 B CN 114524516B CN 202210187138 A CN202210187138 A CN 202210187138A CN 114524516 B CN114524516 B CN 114524516B
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Images
Classifications
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- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F3/00—Biological treatment of water, waste water, or sewage
- C02F3/30—Aerobic and anaerobic processes
- C02F3/301—Aerobic and anaerobic treatment in the same reactor
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- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F11/00—Treatment of sludge; Devices therefor
- C02F11/12—Treatment of sludge; Devices therefor by de-watering, drying or thickening
- C02F11/121—Treatment of sludge; Devices therefor by de-watering, drying or thickening by mechanical de-watering
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- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F9/00—Multistage treatment of water, waste water or sewage
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- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/001—Processes for the treatment of water whereby the filtration technique is of importance
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- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/30—Treatment of water, waste water, or sewage by irradiation
- C02F1/32—Treatment of water, waste water, or sewage by irradiation with ultraviolet light
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- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2101/00—Nature of the contaminant
- C02F2101/30—Organic compounds
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- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2203/00—Apparatus and plants for the biological treatment of water, waste water or sewage
- C02F2203/006—Apparatus and plants for the biological treatment of water, waste water or sewage details of construction, e.g. specially adapted seals, modules, connections
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- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2303/00—Specific treatment goals
- C02F2303/04—Disinfection
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- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02W—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
- Y02W10/00—Technologies for wastewater treatment
- Y02W10/10—Biological treatment of water, waste water, or sewage
Abstract
The invention discloses a biochemical reactor and a sewage treatment method, which solve the problem of large occupied area of a sewage treatment plant in the prior art. A biochemical reactor, comprising: the biochemical reaction structure comprises an anaerobic reaction zone, an anoxic reaction zone and an aerobic reaction zone; wherein, part or all of the anaerobic reaction zone and/or part or all of the anoxic reaction zone are distributed below the aerobic reaction zone. The sewage treatment method adopts the biochemical reactor. In this biochemical reactor, through carrying out integrated design in vertical with anaerobic reaction district, anoxic reaction district and good oxygen reaction district, make full use of vertical space, when guaranteeing the play water effect, very big reduction area.
Description
Technical Field
The invention relates to the technical field of sewage treatment, in particular to the technical field of activated sludge water treatment technology, and specifically relates to a biochemical reactor and a sewage treatment method.
Background
The activated sludge water treatment technology is a main method for biological treatment of wastewater by utilizing biological condensation, adsorption and oxidation of activated sludge to decompose and remove organic pollutants in the wastewater. Mature sewage treatment processes based on the activated sludge process water treatment technology include an A/O process, an A2O process, a multistage AO process, an oxidation ditch process, a Sequencing Batch Reactor (SBR), a CASS process, a Membrane Bioreactor (MBR), a biological fluidized bed, a biological contact oxidation process, a biological aerated filter and the like. The sewage treatment process needs a plurality of functional units connected in series, and the occupied area of the sewage treatment plant is large (the occupied area is generally 0.4-1.6 m 2 /(m 3 D) the construction period is long (6-18 months); in addition, the main structure of the traditional sewage treatment plant generally adopts a reinforced concrete structure, the materials are mainly reinforced concrete and brick-concrete, a large amount of dust and solid waste are inevitably generated during construction, the influence on the surrounding environment is large, and the disassembly (removal) is difficult.
With the continuous acceleration of the urban process in China, the domestic sewage discharge capacity is increased rapidly, and with the continuous improvement of the environmental emission standard, the existing sewage plants are greatly faced with the problem of capacity expansion and upgrading, and part of areas also need new sewage treatment plants. But the land resources in China are increasingly tense, especially in large and medium-sized cities, and enough land is difficult to use for expansion and new construction of sewage plants.
In order to save the occupied area, some sewage plants adopt the construction form of underground sewage treatment plants, but the construction difficulty is large, the construction period is longer, and the investment cost is high; the integrated design construction is adopted in part of sewage treatment plants, namely, all buildings (including equipment rooms, operation rooms, control rooms, office areas, unloading and storage areas) and the like are integrated on the horizontal layout and the vertical layout, for example, the equipment rooms and the operation rooms are designed in the upper space of main structures (sewage treatment units such as anaerobic tanks, anoxic tanks, aerobic tanks and sedimentation tanks), so that certain occupied land can be reduced, but the occupied land can be reduced to a limited extent due to the requirement on the safety distance of all functional units.
In practice, the most effective method for reducing the occupied area is that the occupied area is the main structure which occupies 65% -80% of the total building structure area, so how to perform integrated optimization design on each structure in the vertical space is the most direct method for effectively reducing the occupied area. At present, the aerobic tank and the sediment Chi Shuxiang are overlapped, but the vertical height is limited due to the limitation of conditions such as hydraulic retention time, effective water depth, water pressure, wind pressure of a fan, electromechanical energy consumption and the like, the whole occupied area is reduced to a limited extent on the premise of unchanged total volume, and the occupied area still reaches 0.2-0.4 m at present 2 /(m 3 ·d)。
Disclosure of Invention
In a first aspect, the present invention is directed to providing a biochemical reactor to solve the problem of large occupation area of a sewage treatment plant in the prior art.
In order to achieve the above object of the first aspect, the present invention provides a first biochemical reactor, which has the following technical scheme:
a biochemical reactor, comprising: the biochemical reaction structure comprises an anaerobic reaction zone, an anoxic reaction zone and an aerobic reaction zone; wherein, part or all of the anaerobic reaction zone and/or part or all of the anoxic reaction zone are distributed below the aerobic reaction zone.
In the first biochemical reactor, the anaerobic reaction zone, the anoxic reaction zone and the aerobic reaction zone are integrated in the vertical direction, so that the vertical space is fully utilized, the water outlet effect is ensured, and the occupied area is greatly reduced.
In a second aspect, the present invention aims to provide a biochemical reactor to further reduce the floor space of a sewage treatment plant.
In order to achieve the above object of the second aspect, the present invention provides a second biochemical reactor, which has the following technical scheme:
a biochemical reactor, comprising: the biochemical reaction structure comprises an anaerobic reaction zone, an anoxic reaction zone and an aerobic reaction zone; wherein, part or all of the anaerobic reaction zone and part or all of the anoxic reaction zone are distributed below the aerobic reaction zone and are arranged on the same layer and opposite to each other.
In the second biochemical reactor, part or all of the anaerobic reaction zone and part or all of the anoxic reaction zone are distributed below the aerobic reaction zone and are arranged in the same layer and opposite to each other, so that the integration level is further improved, and the construction period and the building material input cost can be remarkably reduced.
In a third aspect, the present invention aims to provide a biochemical reactor to enhance anaerobic reaction effect while reducing occupation of land.
In order to achieve the above object of the third aspect, the present invention provides a third biochemical reactor, which has the following technical scheme:
a biochemical reactor, comprising: the biochemical reaction structure comprises an anaerobic reaction zone, an anoxic reaction zone and an aerobic reaction zone; wherein, part or all of the anaerobic reaction zone and part or all of the anoxic reaction zone are distributed below the aerobic reaction zone and are separated by a first baffle plate which does not pass through the center of the biochemical reactor.
In the third biochemical reactor, due to the first baffle plates which are obliquely arranged, when the mud-water mixture collides with the first baffle plates, the turbulence effect can be obviously improved, the generation of sludge sedimentation and dead angles is reduced, and the uniform mixing of the activated sludge and the incoming water is ensuredCombining sufficient anaerobic and anaerobic reactions to ensure BOD 5 Degradation effect (of biochemical oxygen demand). Therefore, on the basis of saving occupied space, the third biochemical reactor has better sewage treatment effect.
In a fourth aspect, the present invention aims to provide a biochemical reactor for ease of use and maintenance while reducing the footprint.
In order to achieve the above object of the fourth aspect, the present invention provides a fourth biochemical reactor, which has the following technical scheme:
a biochemical reactor, comprising: the biochemical reaction structure comprises an anaerobic reaction zone, an anoxic reaction zone and an aerobic reaction zone; the anaerobic reaction zone comprises a first cavity and a second cavity, the first cavity is positioned at the side of the aerobic reaction zone and is provided with an upward opening, and the second cavity is positioned below the aerobic reaction zone; the anoxic reaction zone comprises a third cavity and a fourth cavity, the third cavity is positioned at the side of the aerobic reaction zone and is provided with an upward opening, and the fourth cavity is positioned below the aerobic reaction zone.
In the fourth biochemical reactor, the opening end of the first cavity can be used as an inlet for sewage, and the sewage falls into the second cavity from a high position, so that the mixing effect and the turbulence effect of a mud-water mixture in the second cavity can be improved; the first cavity can also be used as an overhaul inlet and an observation port of the anaerobic reaction zone; the third cavity can be used as an overhaul inlet and outlet, an observation port and a reflux port of the anoxic reaction zone; therefore, the fourth biochemical reactor is more convenient to use on the basis of saving occupied space.
In a fifth aspect, the present invention aims to provide a biochemical reactor for ease of use and installation while reducing the footprint.
In order to achieve the above object of the fifth aspect, the present invention provides a fifth biochemical reactor, which has the following technical scheme:
a biochemical reactor, comprising: the biochemical reaction structure comprises an anaerobic reaction zone, an anoxic reaction zone and an aerobic reaction zone; the three-phase separation structure is arranged in the aerobic reaction zone; wherein, part or all of the anaerobic reaction zone and/or part or all of the anoxic reaction zone are distributed below the aerobic reaction zone; a first supporting plate is arranged in the aerobic reaction zone, the left end and the right end of the first supporting plate are connected with the inner wall of the aerobic reaction zone, and the lower end of the first supporting plate is connected with a three-phase separation structure; the aerobic reaction zone comprises a first reaction cavity positioned below the three-phase separation structure and a second reaction cavity positioned beside the three-phase separation structure, and the sedimentation zone and the second reaction cavity above the three-phase separation structure are separated by a first supporting plate.
In the fifth biochemical reactor, the first supporting plate can be used for installing a three-phase separation structure, so that the installation efficiency is improved, and the formed second reaction cavity can also be used as a maintenance access opening and an observation opening of the aerobic reaction zone; by integrating the three-phase separation structure in the aerobic reaction zone, a secondary sedimentation tank can be eliminated, and the occupied area is further remarkably reduced. Therefore, on the basis of saving occupied space, the fifth biochemical reactor is more convenient to install and use.
In a sixth aspect, the present invention aims to provide a biochemical reactor to improve anoxic and aerobic effects while reducing the occupation of space.
In order to achieve the above object of the sixth aspect, the present invention provides a sixth biochemical reactor, which has the following technical scheme:
a biochemical reactor, comprising: the biochemical reaction structure comprises an anaerobic reaction zone, an anoxic reaction zone and an aerobic reaction zone; the three-phase separation structure is arranged in the aerobic reaction zone; the first reflux structure is used for enabling the mud-water mixture at the upper part of the aerobic reaction zone to flow back into the anoxic reaction zone from the aerobic reaction zone; wherein, part or all of the anaerobic reaction zone and/or part or all of the anoxic reaction zone are distributed below the aerobic reaction zone.
In the sixth biochemical reactor, the first reflux structure is arranged, so that the sewage can be subjected to anoxic reaction and aerobic reaction circularly, and the nitrogen removal effect and the phosphorus removal effect are improved; by integrating the three-phase separation structure in the aerobic reaction zone, a secondary sedimentation tank can be eliminated, and the occupied area is further remarkably reduced. Therefore, the sixth biochemical reactor has better sewage treatment effect on the basis of saving occupied space.
In a seventh aspect, the present invention is directed to providing a biochemical reactor to improve water outlet efficiency while reducing floor space.
In order to achieve the above object of the seventh aspect, the present invention provides a seventh biochemical reactor, which has the following technical scheme:
a biochemical reactor, comprising: the biochemical reaction structure comprises an anaerobic reaction zone, an anoxic reaction zone and an aerobic reaction zone; the three-phase separation structure is arranged in the aerobic reaction zone; the drainage structure is arranged above the three-phase separation structure; wherein, part or all of the anaerobic reaction zone and/or part or all of the anoxic reaction zone are distributed below the aerobic reaction zone; the three-phase separation structure comprises a baffle assembly, the baffle assembly is arranged above the aerobic reaction zone and forms a sedimentation zone positioned above the three-phase separation structure, and the baffle assembly is provided with a flow gap which is non-vertical and is communicated with the aerobic reaction zone and the sedimentation zone; the drainage structure comprises an overflow assembly, the overflow assembly is arranged at the upper part of the sedimentation zone, the overflow assembly is provided with overflow grooves which are arranged at intervals, and the supernatant fluid of the sedimentation zone flows into the overflow grooves from overflow ports on the overflow grooves and is discharged to the outside of the biochemical reactor.
In the seventh biochemical reactor, the three-phase separation structure and the drainage structure are arranged above the aerobic reaction zone, so that a secondary sedimentation tank is omitted, occupied space is remarkably saved, the purity and the speed of effluent are remarkably improved, and the treatment efficiency of the post-treatment unit is improved. Therefore, the seventh biochemical reactor has higher water outlet efficiency on the basis of saving occupied space.
In an eighth aspect, the present invention is directed to a sewage treatment system and a sewage treatment method, so as to solve the problem of large occupied area of a sewage treatment plant in the prior art.
In order to achieve the above object of the eighth aspect, the present invention provides a sewage treatment system and a sewage treatment method, which have the following technical solutions:
a sewage treatment system comprising: the pretreatment unit is used for receiving sewage and carrying out solid-liquid separation on the sewage to output first produced water; the biochemical reaction unit is used for sequentially carrying out anaerobic reaction, anoxic reaction, aerobic reaction and three-phase separation on a mud-water mixture comprising the first produced water and the activated sludge and outputting the second produced water and the first sludge; the post-treatment unit is used for carrying out solid-liquid separation and disinfection on the second produced water and outputting the produced water and the second sludge reaching the standards; the sludge concentration unit is used for concentrating the first sludge and the second sludge, outputting clear liquid and mud cakes, and returning the clear liquid to the pre-treatment unit or the biochemical reaction unit; wherein the biochemical reaction unit comprises a biochemical reactor, and the biochemical reactor is any one of the biochemical reactors described in the first aspect to the seventh aspect.
A sewage treatment method employing the biochemical reactor according to any one of the first to seventh aspects, or employing the sewage treatment system.
Proved by verification, the biochemical reactor, the sewage treatment system and the sewage treatment method greatly reduce the occupied area of the structure, and the occupied area can be as low as 0.06-0.08 m 2 /(m 3 D), the biochemical reactor can be assembled by adopting modularized production, so that the civil engineering quantity is small, the matched equipment and accessories are few, the ton water investment is only 1800-2500 yuan, and the construction cost is reduced by 30-50% compared with that of the traditional sewage treatment facilities.
In addition, the biochemical reactor, the sewage treatment system and the sewage treatment method have the following advantages:
(1) The modular design and the prefabricated production can be realized, the modules can be directly transported to the site for assembly, the construction is simple, the construction of a sewage plant with the weight of more than 10 ten thousand tons can be completed within 30 days, and the construction time is greatly shortened; the method is less influenced by site conditions, road transportation conditions and construction conditions; can be flexibly assembled and disassembled, and can be moved and reused in different places, thereby saving resources.
(2) The main body of the assembly structure is made of steel, so that the amount of basic civil engineering is small, and pollution sources such as dust, noise, earthwork, construction waste and the like are greatly reduced; the special steel with the anticorrosive paint is preferably adopted, and the paint film is environment-friendly, nontoxic, low in VOC, tough and wear-resistant, strong in adhesive force, good in physical and mechanical properties, oxidation-resistant and high-temperature-resistant, applicable to different environments and capable of being used for 30-50 years.
(3) The anaerobic action of the microorganism in the anaerobic reaction zone can produce a small amount of methane (the main component is methane CH) 4 ) Part of the odor (e.g. hydrogen sulfide H) 2 S, sulfur dioxide SO 2 ) The gas enters the anoxic reaction zone and the aerobic reaction zone along with the mud-water mixture, methane can be used as a carbon source of microorganisms to a certain extent, hydrogen sulfide, sulfur dioxide and the like can be oxidized and digested under the action of the microorganisms and converted into substances such as sulfate, and finally the gas released into the atmosphere is odorless and harmless, and an exhaust gas collecting and treating system is not required to be added.
(4) The volume of the aerobic reaction zone can be flexibly designed according to the water treatment capacity, the use is flexible and convenient, and the treatment capacity is different from thousands to hundreds of thousands of TPDs.
The invention is further described below with reference to the drawings and detailed description. Additional aspects and advantages of the invention will be set forth in part in the description which follows and, in part, will be obvious from the description, or may be learned by practice of the invention.
Drawings
The accompanying drawings, which form a part hereof, are shown by way of illustration and not of limitation, and in which are shown by way of illustration and description of the invention. In the drawings:
FIG. 1 is a schematic structural diagram of a biochemical reaction structure in a first embodiment of a biochemical reactor according to the present invention.
FIG. 2 is a schematic structural diagram of a biochemical reaction structure in a second embodiment of the biochemical reactor according to the present invention.
FIG. 3 is a schematic structural diagram of a biochemical reaction structure in a third embodiment of the biochemical reactor according to the present invention.
FIG. 4 is a schematic structural diagram of a biochemical reaction structure in a fourth embodiment of the biochemical reactor according to the present invention.
FIG. 5 is a schematic structural diagram of a biochemical reaction structure in a fifth embodiment of the biochemical reactor according to the present invention.
FIG. 6 is a top view showing a biochemical reaction structure in a fifth embodiment of the biochemical reactor according to the present invention.
FIG. 7 is a schematic structural view of a sixth embodiment of the biochemical reactor according to the present invention.
FIG. 8 is a schematic view showing the structure of another embodiment of a baffle plate assembly in a sixth embodiment of a biochemical reactor according to the present invention.
FIG. 9 is a top view of an overflow assembly in a sixth embodiment of a biochemical reactor according to the present invention.
FIG. 10 is a schematic structural view of a seventh embodiment of a biochemical reactor according to the present invention.
FIG. 11 is a schematic structural view of an eighth embodiment of the biochemical reactor according to the present invention.
FIG. 12 is a top view showing a first reflow mechanism and a second reflow mechanism in a ninth embodiment of the biochemical reactor according to the present invention.
FIG. 13 is a side view showing a first reflow mechanism and a second reflow mechanism in a ninth embodiment of the biochemical reactor according to the present invention.
FIG. 14 is a side view of a second reflow mechanism in a ninth embodiment of the biochemical reactor according to the present invention.
FIG. 15 is a schematic view showing the structure of an aeration assembly in the biochemical reactor according to the present invention.
Fig. 16 is a schematic view showing the structure of an embodiment of the sewage treatment system of the present invention.
The relevant marks in the drawings are as follows:
110-anaerobic reaction zone, 111-first chamber, 112-second chamber, 113-first plug flow agitator, 120-anoxic reaction zone, 121-third chamber, 122-fourth chamber, 123-second plug flow agitator, 124-reflux chamber, 130-aerobic reaction zone, 131-first reaction chamber, 132-second reaction chamber, 140-settling zone, 101-first viewing port, 102-second viewing port, 103-third viewing port, 200-housing, 210-first baffle, 220-second baffle, 230-third baffle, 240-bottom plate, 251-first ring beam, 252-second ring beam, 260-notch, 271-air supply pipe, 272-aeration tray, 310-first channel, 320-second channel, 330-sludge discharge port, 400-three-phase separation structure, 401-first baffle unit, 402-second baffle unit, 403-third baffle unit, 410-flap, 411-first plate, 412-second plate, 421-first plate, 422-second plate, 500-drainage structure, 510-overflow tank, 520-secondary header, 530-primary header, 610-first support plate, 620-second support plate, 810-return plate assembly, 811-first return plate, 812-second return plate, 813-third return plate, 820-return pipe, 830-first return pump, 910-second return hole, 920-first horizontal pipe, 930-first riser, 940-second horizontal pipe, 950-second return pump, 710-gas collecting pipeline, 720-second riser, 730-third horizontal pipe, A01-lifting well, A02-first filter equipment, B01-second filter equipment, B02-sterilizing equipment, C01-first concentration equipment and C02-second concentration equipment.
Detailed Description
The present invention will now be described more fully hereinafter with reference to the accompanying drawings. Those of ordinary skill in the art will be able to implement the invention based on these descriptions. Before describing the present invention with reference to the accompanying drawings, it should be noted in particular that:
the technical solutions and technical features provided in the sections including the following description in the present invention may be combined with each other without conflict.
In addition, the embodiments of the present invention referred to in the following description are typically only some, but not all, embodiments of the present invention. Therefore, all other embodiments, which can be made by one of ordinary skill in the art without undue burden, are intended to be within the scope of the present invention, based on the embodiments of the present invention.
Terms and units in relation to the present invention. The terms "comprising," "having," and any variations thereof in the description and claims of the invention and in the relevant sections are intended to cover a non-exclusive inclusion.
FIG. 1 is a schematic structural diagram of a biochemical reaction structure in a first embodiment of a biochemical reactor according to the present invention.
As shown in fig. 1, the biochemical reactor comprises a biochemical reaction structure, the biochemical reaction structure comprises an anaerobic reaction zone 110, an anoxic reaction zone 120 and an aerobic reaction zone 130, wherein all the areas of the anaerobic reaction zone 110 and the anoxic reaction zone 120 are distributed below the aerobic reaction zone 130, and the anaerobic reaction zone 110, the anoxic reaction zone 120 and the aerobic reaction zone 130 are sequentially arranged from bottom to top.
In the biochemical reactor of the first embodiment, the biochemical reaction structure has a layered structure, so that the occupied area of the biochemical reactor is remarkably reduced; the anaerobic reaction zone 110 and the anoxic reaction zone 120 are arranged below the aerobic reaction zone 130, so that the subsequent treatment of the aerobic reaction products is facilitated; the anaerobic reaction zone 110, the anoxic reaction zone 120 and the aerobic reaction zone 130 are sequentially arranged from bottom to top, so that the upward step-by-step flow of the mud-water mixture is facilitated.
FIG. 2 is a schematic structural diagram of a biochemical reaction structure in a second embodiment of the biochemical reactor according to the present invention.
As shown in fig. 2, the biochemical reactor includes a biochemical reaction structure, the biochemical reaction structure includes an anaerobic reaction zone 110, an anoxic reaction zone 120 and an aerobic reaction zone 130, wherein a partial area of the anaerobic reaction zone 110 and a partial area of the anoxic reaction zone 120 are distributed below the aerobic reaction zone 130, and the anaerobic reaction zone 110, the anoxic reaction zone 120 and the aerobic reaction zone 130 are sequentially arranged from bottom to top.
In comparison with the first embodiment, the partial areas of the anaerobic reaction zone 110 and the anoxic reaction zone 120 in the biochemical reactor of the second embodiment extend to the outside of the aerobic reaction zone 130, and the extended partial areas may serve as a service inlet and a viewing port.
FIG. 3 is a schematic structural diagram of a biochemical reaction structure in a third embodiment of the biochemical reactor according to the present invention.
As shown in fig. 3, the biochemical reactor comprises a biochemical reaction structure, the biochemical reaction structure comprises an anaerobic reaction zone 110, an anoxic reaction zone 120 and an aerobic reaction zone 130, wherein all the areas of the anaerobic reaction zone 110 and the anoxic reaction zone 120 are distributed below the aerobic reaction zone 130 and are arranged in the same layer and opposite to each other.
Compared with the first embodiment, the biochemical reactor of the third embodiment has more optimized integration level, and can remarkably reduce the construction period and the building material input cost; and, the anaerobic reaction zone 110 and the anoxic reaction zone 120 are arranged on the same layer, so that the mud-water mixture can conveniently move from the anaerobic reaction zone 110 to the anoxic reaction zone 120, and the energy consumption required by the flow of the mud-water mixture is reduced.
FIG. 4 is a schematic structural diagram of a biochemical reaction structure in a fourth embodiment of the biochemical reactor according to the present invention.
As shown in fig. 4, the biochemical reactor includes a biochemical reaction structure, which includes an anaerobic reaction zone 110, an anoxic reaction zone 120 and an aerobic reaction zone 130, wherein a partial area of the anaerobic reaction zone 110 and a partial area of the anoxic reaction zone 120 are distributed below the aerobic reaction zone 130 and are arranged in the same layer and opposite to each other.
In comparison with the third embodiment, the partial areas of the anaerobic reaction zone 110 and the anoxic reaction zone 120 in the biochemical reactor of the fourth embodiment extend to the outside of the aerobic reaction zone 130, and the extended partial areas may serve as a service inlet and a viewing port.
FIG. 5 is a schematic structural diagram of a biochemical reaction structure in a fifth embodiment of the biochemical reactor according to the present invention.
As shown in fig. 5, the biochemical reactor comprises a biochemical reaction structure, the biochemical reaction structure comprises an anaerobic reaction zone 110, an anoxic reaction zone 120 and an aerobic reaction zone 130, the anaerobic reaction zone 110 comprises a first cavity 111 and a second cavity 112, the first cavity 111 is positioned at the side of the aerobic reaction zone 130 and has an upward opening, and the second cavity 112 is positioned below the aerobic reaction zone 130; the anoxic reaction zone 120 comprises a third cavity 121 and a fourth cavity 122, the third cavity 121 is located at the side of the aerobic reaction zone 130 and has an upward opening, and the fourth cavity 122 is located below the aerobic reaction zone 130; the second cavity 112 and the fourth cavity 122 are disposed in the same layer and opposite.
Compared with the fourth embodiment, the first cavity 111 and the third cavity 121 in the biochemical reactor of the fifth embodiment extend upwards to be level with the aerobic reaction zone 130, which is more convenient for processing, manufacturing and use; in addition, sewage falls into the second cavity 112 from a high place (the opening end of the first cavity 111), so that the mixing effect and the turbulence effect of the mud-water mixture in the second cavity 112 can be improved; meanwhile, when the nitrified liquid in the aerobic reaction zone 130 flows back to the fourth cavity 122 from the upper side of the third cavity 121, the anoxic reaction effect in the fourth cavity 122 can be improved in a manner that the high place falls into the fourth cavity. Likewise, the open ends of the second and fourth chambers 112, 122 can also function as service and viewing ports (i.e., the first viewing port 101 for viewing the anaerobic reaction zone 110 and the second viewing port 102 for viewing the anoxic reaction zone 120).
Among the above-described five embodiments, the biochemical reactor of the fifth embodiment has the best integration effect and use effect, and thus, other structures of the biochemical reactor of the fifth embodiment are further described in detail below. The method comprises the following steps:
the volume ratio of the second cavity 112 to the fourth cavity 122 is preferably 1: (2-10) to meet the requirements of various water quality of inlet water and water quality of outlet water; in particular implementations, the volume ratio of the second cavity 112 to the fourth cavity 122 may be, but is not limited to being, any of 1:2, 1:3, 1:4, 1:5, 1:6, 1:7, 1:8, 1:9, 1:10.
A first push flow stirrer 113 is arranged at the bottom of the first cavity 111 to promote the mixing effect of the mud-water mixture, and the first push flow stirrer 113 can be one or more; the bottom of the third cavity 121 is provided with a second plug-flow mixer 123 to enhance the mixing effect of the mud-water mixture, and the number of the second plug-flow mixer 123 may be one or more.
FIG. 6 is a top view showing a biochemical reaction structure in a fifth embodiment of the biochemical reactor according to the present invention.
As shown in fig. 6, the biochemical reaction structure further includes a housing 200, a second partition 220, and a third partition 230; the anaerobic reaction zone 110, the anoxic reaction zone 120 and the aerobic reaction zone 130 are integrated in the housing 200; the left and right ends of the second partition 220 are connected with the side wall of the shell 200, the lower end is connected with the bottom plate 240 of the aerobic reaction zone 130, and the first cavity 111 and the aerobic reaction zone 130 are separated by the second partition 220; the left and right ends of the third partition 230 are connected to the side wall of the casing 200, the lower end is connected to the bottom plate 240 of the aerobic reaction zone 130, and the third cavity 121 and the aerobic reaction zone 130 are separated by the third partition 230. Therefore, the anaerobic reaction zone 110, the anoxic reaction zone 120 and the aerobic reaction zone 130 can be formed by welding the housing 200, the second partition 220, the third partition 230 and the bottom plate 240, and the installation is more convenient.
The housing 200 may be prismatic or cylindrical; preferably, the cylindrical shell 200 is adopted, so that firstly, the opening sizes of the first cavity 111, the third cavity 121 and the aerobic reaction zone 130 are convenient to flexibly control, secondly, the mud-water mixture flows in the cylindrical container and is not easy to generate dead angles, the effective use area in unit area is larger, thirdly, the cylindrical structure is more convenient to process and assemble, fourthly, when being impacted by water flow, the stress is more uniform, and the structural stability is stronger.
The second and third partitions 220 and 230 are symmetrically disposed at both sides of the aerobic reaction zone 130, and the second and third partitions 220 and 230 are vertically disposed, thereby facilitating rapid installation.
The second chamber 112 and the fourth chamber 122 are preferably divided and disposed opposite to each other by the first partition 210, and both right and left ends of the first partition 210 are connected to the side wall of the casing 200, the lower end is connected to the bottom of the casing 200, and the upper end is connected to the bottom plate 240 of the aerobic reaction zone 130, thereby reducing material costs and further simplifying installation.
The projection of the connection part of one end of the first partition board 210 and the shell 200 and the projection of the connection part of one end of the second partition board 220 and the shell 200 coincide, and the included angle 1 between the first partition board 210 and the second partition board 220 is 40-50 degrees, at this time, when the mud-water mixture contacts and collides with the first partition board 210 which is obliquely arranged under the action of the first plug-flow stirrer 113, the resultant force can enhance the turbulence effect, reduce the generation of the sedimentation and dead angle of the activated sludge, and ensure the uniform mixing of the activated sludge and the incoming water, thereby ensuring the efficiency of the biochemical reaction; in specific implementation, the angle 1 between the first separator 210 and the second separator 220 may be, but is not limited to, any one of 40 °, 41 °, 42 °, 43 °, 44 °, 45 °, 46 °, 47 °, 48 °, 49 °, and 50 °.
The first baffle 210 is preferably a wave-shaped plate that further enhances the turbulence effect compared to a straight plate.
The first partition 210 is provided with a first channel 310 for the mud-water mixture to flow from the second cavity 112 into the fourth cavity 122, and the first channel 310 is arranged on the first partition 210 far away from the second partition 220, so that the flow path of the mud-water mixture is prolonged, and the anaerobic reaction effect is improved. The first channel 310 is preferably a slot, i.e. the cross-section of the first channel 310 is rectangular, so that the mud-water mixture forms a vortex when passing through the first channel 310, thereby uniformly distributing the flow in the fourth chamber 122. The first channel 310 is 0.4-0.6 m away from the bottom of the casing 200 and 0.4-0.8 m away from the side wall of the casing 200, so that the flow distribution effect is optimal; in particular embodiments, the first channel 310 may be, but is not limited to, any of 0.4m, 0.5m, and 0.6m from the bottom of the housing 200, and the first channel 310 may be, but is not limited to, any of 0.4m, 0.5m, 0.6m, 0.7m, and 0.8m from the sidewall of the housing 200.
The second channel 320 for the mud-water mixture to flow into the aerobic reaction zone 130 from the fourth cavity 122 is arranged on the bottom plate 240 of the aerobic reaction zone 130 and the aeration component, and the second channel 320 is arranged on the bottom plate 240 and the aeration component far away from the third cavity 121, so that the flow path of the mud-water mixture is prolonged, and the anoxic reaction effect is improved. The second channel 320 is preferably a coin slot, so that the mud-water mixture forms a vortex when passing through the second channel 320, thereby uniformly distributing the flow in the aerobic reaction zone 130. The connecting line between the center of the second channel 320 and the side edge of the second partition plate 220 is perpendicular to the second partition plate 220, and the length of the connecting line is 3.6-4.4 m, so that a beneficial reflection angle can be formed by the arrangement, the turbulent flow of the mud-water mixture is facilitated, dead angles are reduced, and the flow distribution effect is improved; in particular, the length of the wiring may be, but is not limited to, any of 3.6m, 3.8m, 4m, 4.2m, 4.4 m.
The side wall of the shell 200 is provided with a sludge discharge port 330 for the sludge water mixture to flow from the aerobic reaction zone 130 to the outside of the shell 200, preferably, the sludge discharge port 330 is arranged on the side wall of the shell 200 above the anaerobic reaction zone 110, further preferably, the included angle 2 between the connecting line of the sludge discharge port 330 and the center of the shell 200 and the connecting line of the center of the second partition plate 220 and the center of the third partition plate 230 is 40-50 degrees, thereby prolonging the flow path of the sludge water mixture and improving the aerobic reaction effect; the angle 2 of the line connecting the sludge discharge port 330 and the center of the housing 200 and the line connecting the center of the second separator 220 and the third separator 230 may be, but not limited to, any one of 40 °, 41 °, 42 °, 43 °, 44 °, 45 °, 46 °, 47 °, 48 °, 49 °, 50 °.
FIG. 7 is a schematic structural view of a sixth embodiment of the biochemical reactor according to the present invention.
As shown in fig. 7, the biochemical reactor of the sixth embodiment further has a three-phase separation structure 400 and a drainage structure 500, on the basis of the fifth embodiment; the three-phase separation structure 400 comprises a baffle assembly which is arranged above the aerobic reaction zone 130 and forms a sedimentation zone 140 positioned above the three-phase separation structure 400, and the baffle assembly is provided with a flow gap which is non-vertical and is communicated with the aerobic reaction zone 130 and the sedimentation zone 140; the drainage structure 500 includes an overflow assembly installed at the upper portion of the settling zone 140, the overflow assembly having overflow grooves 510 arranged at intervals, and supernatant liquid of the settling zone 140 flowing into the overflow grooves 510 from overflow ports on the overflow grooves 510 and being discharged to the outside of the biochemical reactor.
Therefore, under the action of the aeration component, the bubbles slowly rise from the bottom of the aerobic reaction zone 130 with the mud-water mixture, when the bubbles contact the three-phase separation structure 400, the activated sludge in the mud-water mixture is reflected when the activated sludge contacts the baffle of the three-phase separation structure 400, the particles are continuously collided and flocculated, the particles are gradually increased, the particles are finally settled to the lower part of the aerobic reaction zone 130 due to self gravity, and the water in the mud-water mixture continuously rises until overflows into the overflow groove 510 and is discharged, so that the three-phase separation of solid, liquid and gas is finally realized. Therefore, the sewage treatment system with the biochemical reactor can eliminate the use of a secondary sedimentation tank or a sedimentation tank with larger occupied area, thereby further remarkably reducing the occupied area.
The baffle assembly is provided with a first baffle unit 401 and a second baffle unit 402 which are arranged in a layered mode, the distance d1 between the first baffle unit 401 and the second baffle unit 402 is 550-700 mm, the first baffle unit 401 and the second baffle unit 402 are provided with folded plates 410 which are arranged at intervals in a staggered mode, and the folded plates 410 are provided with a first plate 411 and a second plate 412 which are connected with each other, the openings of the folded plates are downward, and therefore three-phase separation effect is good. The included angle between the first plate 411 and the second plate 412 is 55-65 degrees, and the width d2 of the first plate 411 and the second plate 412 is 600-700 mm, so that the optimal three-phase separation efficiency can be obtained; in specific implementations, the distance d1 may be, but not limited to, any one of 550mm, 580mm, 600mm, 620mm, 640mm, 660mm, 680mm, 700mm, the included angle between the first plate 411 and the second plate 412 may be, but not limited to, any one of 55 °, 57 °, 59 °, 60 °, 63 °, 65 °, and the width d2 may be, but not limited to, any one of 600mm, 620mm, 640mm, 660mm, 680mm, 700 mm.
FIG. 8 is a schematic view showing the structure of another embodiment of a baffle plate assembly in a sixth embodiment of a biochemical reactor according to the present invention.
As shown in fig. 8, the baffle assembly further comprises a third baffle unit 403 disposed between the first baffle unit 401 and the second baffle unit 402, the third baffle unit 403 having a first flat plate 421 and a second flat plate 422 arranged at intervals, the first flat plate 421 and the first plate 411 having a width d3 of 600 to 700mm, the first flat plate 421 being disposed in parallel with the first plate 411, the second flat plate 422 being disposed in parallel with the second plate 412, and a distance d4 between upper ends of the first flat plate 421 and the second flat plate 422 being 200 to 300mm; therefore, the three-phase separation effect is further improved; in specific implementations, the width d3 may be, but is not limited to, any of 600mm, 620mm, 640mm, 660mm, 680mm, and 700mm, and the pitch d4 may be, but is not limited to, any of 200mm, 220mm, 240mm, 260mm, 280mm, and 300 mm.
The width d5 of the gap between the first plate 411 and the first plate 421 and the gap between the second plate 412 and the second plate 422 are 50 to 100mm, and the width d6 of the gap between the first plate 421 and the second plate 412 and the gap between the second plate 422 and the first plate 411 are 50 to 100mm, so that the three-phase separation effect is optimal; in particular, the width d5 and the width d6 may be, but are not limited to, any one of 50mm, 60mm, 70mm, 80mm, 90mm, 100 mm.
FIG. 9 is a top view of an overflow assembly in a sixth embodiment of a biochemical reactor according to the present invention.
As shown in fig. 9, the overflow assembly further includes a secondary water collecting pipe 520 arranged at intervals, the secondary water collecting pipe 520 being perpendicular to the overflow tank 510 and communicating with the overflow tank 510, and a main water collecting pipe 530, an end of the secondary water collecting pipe 520 arranged at intervals being connected to the main water collecting pipe 530. Thereby, the uniform treatment of the effluent is facilitated.
Preferably, the distance between the sludge discharge port 330 and the bottom of the three-phase separation structure 400 is not less than 0.5m, thereby reducing the outflow amount of nitrifying liquid; the interval between the sludge discharge port 330 and the bottom of the three-phase separation structure 400 is preferably 1m.
FIG. 10 is a schematic structural view of a seventh embodiment of a biochemical reactor according to the present invention.
As shown in fig. 10, the biochemical reactor of the seventh embodiment further has a first support plate 610, both right and left ends of the first support plate 610 are connected to the inner wall of the aerobic reaction zone 130, and the lower end is connected to the three-phase separation structure 400, the aerobic reaction zone 130 includes a first reaction chamber 131 located below the three-phase separation structure 400 and a second reaction chamber 132 located at the side of the three-phase separation structure 400, and the settling zone 140 and the second reaction chamber 132 above the three-phase separation structure 400 are separately disposed by the first support plate 610.
Thus, the first support plate 610 may be used to install the three-phase separation structure 400, to enhance installation efficiency, and the formed second reaction chamber 132 may also serve as a service outlet and a viewing port of the aerobic reaction zone 130 (i.e., to view the third viewing port 103 of the aerobic reaction zone 130).
FIG. 11 is a schematic structural view of an eighth embodiment of the biochemical reactor according to the present invention.
As shown in fig. 11, the biochemical reactor according to the eighth embodiment further has a second support plate 620 on the basis of the seventh embodiment, wherein the left and right ends of the second support plate 620 are connected to the side wall of the casing 200, the lower ends thereof are connected to the three-phase separation structure 400, the first support plate 610 and the second support plate 620 are parallel, the first support plate 610 and the second support plate 620 are symmetrically disposed at both sides of the aerobic reaction zone 130, the first support plate 610 and the second support plate 620 are vertically disposed, and the three-phase separation structure 400 and the drainage structure 500 are installed in an installation cavity defined by the casing 200, the second partition 220, the third partition 230, the first support plate 610 and the second support plate 620.
Thereby, the manufacturing and installation of the three-phase separation structure 400 and the drainage structure 500 are facilitated. Likewise, a second reaction chamber 132 (or a third viewing port 103) may also be formed between the second support plates 620.
To further simplify the installation of the three-phase separation structure 400 and the drainage structure 500, the installation cavity is provided with a first ring beam 251 adapted to the three-phase separation structure 400 and a second ring beam 252 adapted to the drainage structure 500, the first ring beam 251 is welded or bolted to the three-phase separation structure 400, the second ring beam 252 is welded or bolted to the drainage structure 500, and the connection line between the centers of the second partition 220 and the third partition 230 is perpendicular to the connection line between the centers of the first support plate 610 and the second support plate 620.
FIG. 12 is a top view showing a first reflow mechanism and a second reflow mechanism in a ninth embodiment of the biochemical reactor according to the present invention. FIG. 13 is a side view showing a first reflow mechanism and a second reflow mechanism in a ninth embodiment of the biochemical reactor according to the present invention. FIG. 14 is a side view of a second reflow mechanism in a ninth embodiment of the biochemical reactor according to the present invention.
As shown in fig. 12 to 14, in addition to the eighth embodiment, the biochemical reactor of the ninth embodiment further has a first reflux structure for refluxing the sludge-water mixture from the aerobic reaction zone 130 into the anaerobic reaction zone 120 and a second reflux structure for refluxing the sludge-water mixture from the anaerobic reaction zone 120 into the anaerobic reaction zone 110; the first reflow structure includes a first reflow mechanism and a second reflow mechanism.
The first reflux mechanism is used for refluxing the mud-water mixture at the upper part of the second reaction cavity 132 from the second reaction cavity 132 into the anoxic reaction zone 120; thereby due to the second reaction chamber132 is significantly less than the first reaction chamber 131, thereby enabling as much of the nitrifying liquid (i.e., a sludge-water mixture having a low sludge content, nitrifying liquid containing nitrate Nitrogen (NO) 3 -N) and nitrite Nitrogen (NO) 2 -N)) back to anoxic reaction zone 120.
The anoxic reaction zone 120 further includes a return chamber 124, the return chamber 124 being located laterally of the second reaction chamber 132; the first return mechanism is used for returning the mud-water mixture from the second reaction chamber 132 into the return chamber 124; specifically, the bottom plate 240 and the aeration component of the aerobic reaction zone 130 are provided with a notch 260, the first backflow mechanism is provided with a backflow plate component 810, the bottom of the backflow plate component 810 is connected with the notch 260 and forms a backflow cavity 124 communicated with the fourth cavity 122 through the notch 260, the backflow cavity 124 and the second reaction cavity 132 are arranged at intervals through the backflow plate component 810, and the backflow plate component 810 is provided with a first backflow hole for backflow of the mud-water mixture from the second reaction cavity 132 into the backflow cavity 124, a backflow pipe 820 matched with the first backflow hole and a first backflow pump 830; therefore, the reflux is realized, and the processing and the manufacturing are convenient.
The notch 260 is rectangular, and the reflow board assembly 810 includes a first reflow board 811, a second reflow board 812 and a third reflow board 813 connected end to end, and the first reflow hole is formed on the upper portion of the first reflow board 811 or the third reflow board 813, thereby facilitating quick installation. In order to reduce dead space, the second reflow plate 812 and the first support plate 610 are preferably placed in contact.
The widths of the first return plate 811, the second return plate 812 and the third return plate 813 are 1.5 to 2m, thereby facilitating installation and maintenance of the first return mechanism.
The second reflux mechanism comprises a gas collecting pipeline 710, a second ascending pipe 720 and a third horizontal pipe 730, wherein the gas collecting pipeline 710 is connected with the baffle assembly and is communicated with the aerobic reaction zone 130, an outlet of the third horizontal pipe 730 is positioned above the third cavity 121, and a mud-water mixture (mainly nitrifying liquid) flowing out of the gas collecting pipeline 710 flows into the anoxic reaction zone 120 from above the third cavity 121. Therefore, when the bubbles of the aeration assembly hit the plate body of the baffle assembly, the bubbles are deflected to the periphery of the plate body and then pass through the water layer to enter the gas collecting pipeline 710 to be discharged, and partial negative pressure is formed in the aerobic reaction zone 130 due to the discharge of the gas, so that the gas stripping effect is generated, and part of the sludge-water mixture in the aerobic reaction zone 130 flows out through the gas collecting pipeline 710 under the gas stripping effect and flows back to the third cavity 121 of the anoxic reaction zone 120 through the second riser 720 and the third horizontal pipe 730. The third horizontal pipe 730 is 0.5-1 m higher than the overflow tank 510 to stably reflux the sludge-water mixture.
The second return structure includes a second return hole 910 provided on the first partition 210, and the second return hole 910 is preferably provided on the first partition 210 adjacent to the second partition 220, whereby the sludge-water mixture, which is convenient for the return, sufficiently performs anaerobic reaction. And, the second backflow structure further comprises a first horizontal pipe 920, a first rising pipe 930, a second horizontal pipe 940 and a second backflow pump 950, which are sequentially connected with the second backflow hole 910, wherein an inlet of the second horizontal pipe 940 (i.e. the second backflow pump 950) is located at the lower part of the backflow cavity 124, so that a part of the sludge-water mixture from the anoxic reaction zone 120 above the second horizontal pipe 940 can flow back to the anaerobic reaction zone 110, which is helpful for improving the biochemical reaction effect.
The second return hole 910 is 0.8-1.2 m away from the bottom of the casing 200 and 1.8-2.2 m away from the sidewall of the casing 200, thereby helping the returned mud-water mixture to be uniformly distributed in the anaerobic reaction zone 110; in particular, the second return hole 910 may be, but not limited to, any one of 0.8m, 0.9m, 1m, 1.1m, 1.2m from the bottom of the case 200, and the second return hole 910 may be, but not limited to, any one of 1.8m, 1.9m, 2m, 2.1m, 2.2m from the sidewall of the case 200.
In the biochemical reactor of the above nine embodiments:
the aeration components are arranged on the bottom plate 240 of the aerobic reaction zone 130, and are arranged on the bottom plate 240 of the aerobic reaction zone 130 through brackets, and as shown in fig. 15, the aeration components comprise air supply pipes 271 arranged on the brackets and aeration discs 272 communicated with the air supply pipes 271, and the air supply pipes 271 are arranged at intervals of 0.5-0.7 m in the transverse direction and the vertical direction. The distance between the support and the bottom plate 240 is 0.2-0.3 m, thereby not only reducing the dead angle of activated sludge deposition between the aeration assembly and the bottom plate 240, but also enabling bubbles to fully contact with the sludge-water mixture.
In order to ensure the dephosphorization effect, a chemical dephosphorization reagent feeding device can be arranged, so that when the biochemical dephosphorization effect is poor, chemical dephosphorization reagent is fed into the aerobic reaction zone 130 for removal, and most of phosphorus is finally removed along with the discharge of the surplus sludge.
The aerobic reaction zone 130 is surrounded by the second partition 220, the third partition 230 and the casing 200 (i.e., four corners are tangential), the sedimentation zone 140 is surrounded by the second partition 220, the third partition 230, the first support plate 610, the second support plate 620 and the casing 200, and if the volumes of the aerobic reaction zone 130 and the sedimentation zone 140 (such as a scene of great water treatment capacity) need to be increased, the width of the partition can be reduced in addition to the depth; when the width of the partition plate is reduced, in order to facilitate the installation of the three-phase separation structure 400 and the drainage structure 500, the number of partition plates and/or support plates may be appropriately increased (i.e., may be designed as a hexagonal cut, an octagonal cut, a twelve-angle cut, etc., as the case may be).
The top of the housing 200 is provided with hallways and fences, and the outer wall of the housing is provided with stairs and fences leading to the hallways, thereby facilitating use, observation and maintenance.
Fig. 16 is a schematic view showing the structure of an embodiment of the sewage treatment system of the present invention.
As shown in fig. 16, the sewage treatment system includes a pre-treatment unit, a biochemical reaction unit, a post-treatment unit, and a sludge concentration unit, wherein the biochemical reaction unit includes one or more biochemical reactors, and the biochemical reactors are any one of the biochemical reactors of the first to ninth embodiments, and preferably the biochemical reactor of the ninth embodiment is used.
The pre-treatment unit is used for receiving sewage and carrying out solid-liquid separation on the sewage to output first produced water; specifically, the pre-treatment unit comprises a lift well a01 and a first filtering device a02; the lifting well A01 is used for receiving and storing sewage, preferably sewage from an urban sewage pipe network; the first filtering equipment A02 is used for filtering sewage and outputting first produced water, the first filtering equipment A02 is preferably a grating assembly, and the grating assembly is preferably a coarse grating and a fine grating which are sequentially arranged. The mud-water mixture comprising the first produced water and the activated sludge is subjected to anaerobic reaction, anoxic reaction, aerobic reaction and three-phase separation in the biochemical reaction unit in sequence to obtain the second produced water and the first sludge.
The post-treatment unit is used for carrying out solid-liquid separation and disinfection on the second produced water and outputting the produced water and the second sludge reaching the standard; specifically, the post-processing unit includes a second filtering device B01 and a sterilizing device B02; the second filtering device B01 is used for filtering the second produced water and outputting third produced water and second sludge, and the second filtering device B01 is preferably a fiber rotary disc filter; the disinfection equipment B02 is used for disinfecting third produced water and outputting produced water reaching standards, and the disinfection equipment B02 is preferably an ultraviolet disinfection canal. Through verification, the standard produced water can reach the first-level A standard in GB18918-2002 of pollutant emission standards of urban sewage treatment plants and the IV standard in GB3838-2002 of surface water environment quality standards, and can be directly discharged.
The sludge concentration unit is used for concentrating the first sludge and the second sludge, outputting clear liquid and mud cakes, and returning the clear liquid to the pre-treatment unit or the biochemical reaction unit; specifically, the sludge concentration unit includes a first concentration device C01 and a second concentration device C02; the first concentration device C01 is used for naturally settling the first sludge and the second sludge, outputting supernatant and settled sludge, and refluxing the supernatant to the pre-treatment unit or the biochemical reaction unit, wherein the first concentration device C01 is preferably a sludge concentration tank; the second concentration device C02 is used for dehydrating settled sludge, outputting filtrate and mud cakes, and refluxing the filtrate to a pre-treatment unit or a biochemical reaction unit, wherein the second concentration device C02 is preferably a sludge dehydrator.
An embodiment of the sewage treatment method of the present invention is to employ any one of the biochemical reactors of the first to ninth embodiments described above, or to employ the sewage treatment system described above.
The content of the present invention is described above. Those of ordinary skill in the art will be able to implement the invention based on these descriptions. Based on the foregoing, all other embodiments that may be obtained by one of ordinary skill in the art without undue burden are within the scope of the present invention.
Claims (12)
1. The biochemical reactor is characterized in that: comprising the following steps:
a biochemical reaction structure comprising an anaerobic reaction zone (110), an anoxic reaction zone (120) and an aerobic reaction zone (130);
wherein, a partial area of the anaerobic reaction zone (110) and a partial area of the anoxic reaction zone (120) are distributed below the aerobic reaction zone (130) and are arranged on the same layer;
the anaerobic reaction zone (110) comprises a first cavity (111) and a second cavity (112), the first cavity (111) is positioned at the side of the aerobic reaction zone (130) and is provided with an upward opening, and the second cavity (112) is positioned below the aerobic reaction zone (130);
the anoxic reaction zone (120) comprises a third cavity (121) and a fourth cavity (122), the third cavity (121) is positioned at the side of the aerobic reaction zone (130) and is provided with an upward opening, and the fourth cavity (122) is positioned below the aerobic reaction zone (130);
The first cavity (111) and the third cavity (121) extend upwards to be level with the aerobic reaction zone (130);
the biochemical reaction structure further comprises:
a housing (200), wherein the anaerobic reaction zone (110), the anoxic reaction zone (120) and the aerobic reaction zone (130) are integrated in the housing (200);
the left end and the right end of the first partition plate (210) are connected with the side wall of the shell (200), the lower end of the first partition plate is connected with the bottom of the shell (200), the upper end of the first partition plate is connected with the bottom plate (240) of the aerobic reaction zone (130), and the second cavity (112) and the fourth cavity (122) are separated and arranged through the first partition plate (210);
the left end and the right end of the second partition plate (220) are connected with the side wall of the shell (200), the lower end of the second partition plate is connected with the bottom plate (240) of the aerobic reaction zone (130), and the first cavity (111) and the aerobic reaction zone (130) are separated by the second partition plate (220);
the left end and the right end of the third partition plate (230) are connected with the side wall of the shell (200), the lower end of the third partition plate is connected with the bottom plate (240) of the aerobic reaction zone (130), and the third cavity (121) and the aerobic reaction zone (130) are separated by the third partition plate (230);
a first channel (310) for the mud-water mixture to flow from the second cavity (112) into the fourth cavity (122) is arranged on the first partition board (210), and the first channel (310) is arranged on the first partition board (210) far away from the second partition board (220); the included angle between the first clapboard (210) and the second clapboard (220) is 40-50 degrees;
The second clapboard (220) and the third clapboard (230) are symmetrically arranged at two sides of the aerobic reaction zone (130);
a second channel (320) for the mud-water mixture to flow into the aerobic reaction zone (130) from the fourth cavity (122) is arranged on the bottom plate (240) and the aeration component of the aerobic reaction zone (130);
the second channel (320) is arranged on the bottom plate (240) far away from the third cavity (121) and the aeration component;
nitrifying liquid in the aerobic reaction zone (130) flows back to the fourth cavity (122) from the upper part of the third cavity (121).
2. The biochemical reactor according to claim 1, wherein: a first plug-flow stirrer (113) is arranged in the first cavity (111); a second plug flow stirrer (123) is arranged in the third cavity (121); the volume ratio of the second cavity (112) to the fourth cavity (122) is 1: (2-10).
3. The biochemical reactor according to claim 1, wherein: the housing (200) is cylindrical.
4. The biochemical reactor according to claim 1, wherein: the first channel (310) and/or the second channel (320) are coin slots.
5. The biochemical reactor according to claim 1, wherein: the biochemical reactor further comprises:
a first return structure for returning the slurry-water mixture from the aerobic reaction zone (130) to the anoxic reaction zone (120);
And a second return structure for returning the sludge-water mixture from the anoxic reaction zone (120) to the anaerobic reaction zone (110).
6. The biochemical reactor according to claim 5, wherein: the second return structure includes a second return aperture (910) provided in the first separator (210).
7. The biochemical reactor according to claim 6, wherein: the second return hole (910) is provided on the first separator (210) adjacent to the second separator (220).
8. The biochemical reactor according to claim 1, wherein: a sludge discharge port (330) through which a sludge-water mixture flows from the aerobic reaction zone (130) to the outside of the shell (200) is arranged on the side wall of the shell (200).
9. The biochemical reactor according to claim 8, wherein: the sludge discharge port (330) is arranged on the side wall of the shell (200) above the anaerobic reaction zone (110).
10. The biochemical reactor according to claim 9, wherein: the included angle between the connecting line of the sludge discharge port (330) and the center of the shell (200) and the connecting line of the center of the second partition plate (220) and the center of the third partition plate (230) is 40-50 degrees.
11. The biochemical reactor according to claim 1, wherein: the biochemical reactor further comprises:
A three-phase separation structure (400), the three-phase separation structure (400) comprising a baffle assembly, the baffle assembly being mounted above the aerobic reaction zone (130) and forming a settling zone (140) above the three-phase separation structure (400), the baffle assembly having a non-vertical flow gap communicating the aerobic reaction zone (130) and the settling zone (140);
the drainage structure (500), the drainage structure (500) includes overflow subassembly, overflow subassembly installs in the upper portion of sedimentation zone (140), overflow subassembly has overflow launder (510) of interval arrangement, and the supernatant of sedimentation zone (140) is discharged outside the biochemical reactor after overflow mouth inflow overflow launder (510) on overflow launder (510).
12. The sewage treatment method is characterized in that: use of a biochemical reactor according to any one of claims 1 to 11.
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| US6309553B1 (en) * | 1999-09-28 | 2001-10-30 | Biothane Corporation | Phase separator having multiple separation units, upflow reactor apparatus, and methods for phase separation |
| KR100446107B1 (en) * | 2002-07-23 | 2004-08-30 | 최흥진 | Bioreactor for Treating Wastewater |
| CN102153239B (en) * | 2011-04-19 | 2012-07-25 | 中冶南方工程技术有限公司 | Process and system for carrying out high-efficiency denitrification and dephosphorization treatment on urban sewage |
| CN202322548U (en) * | 2011-09-08 | 2012-07-11 | 东莞市开源环境科技有限公司 | Anerobic, anoxic, aerobic tanks and bio-membrane reactor combined device for floating boat aeration |
| CN107417032A (en) * | 2017-05-10 | 2017-12-01 | 安阳工学院 | A kind of sewage disposal system and sewage water treatment method |
| CN208120821U (en) * | 2018-03-12 | 2018-11-20 | 苏州科特环保股份有限公司 | A kind of anaerobism, anoxic, aerobic integratedization reactor |
| CN208532540U (en) * | 2018-05-29 | 2019-02-22 | 四川玖清环保设备有限公司 | Integrated sewage treating apparatus |
| CN109516553A (en) * | 2018-11-26 | 2019-03-26 | 上海泓济环保科技股份有限公司 | Efficient anaerobic denitrification organisms reactor |
| CN209537232U (en) * | 2018-12-27 | 2019-10-25 | 北京首创清源环境科技有限公司 | Biochemical synthesis pond |
| CN210656359U (en) * | 2019-08-23 | 2020-06-02 | 广州鹏凯环境科技股份有限公司 | Synchronous short-cut nitrification and denitrification water treatment device |
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