CN112321077A - High-efficient sediment and denitrification sewage treatment system - Google Patents

High-efficient sediment and denitrification sewage treatment system Download PDF

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Publication number
CN112321077A
CN112321077A CN202011180663.8A CN202011180663A CN112321077A CN 112321077 A CN112321077 A CN 112321077A CN 202011180663 A CN202011180663 A CN 202011180663A CN 112321077 A CN112321077 A CN 112321077A
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China
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water
denitrification
tank
water inlet
filter
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CN202011180663.8A
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Chinese (zh)
Inventor
黄廷伟
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Shenzhen Duoerwei Environmental Technology Co ltd
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Shenzhen Duoerwei Environmental Technology Co ltd
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Priority to CN202011180663.8A priority Critical patent/CN112321077A/en
Publication of CN112321077A publication Critical patent/CN112321077A/en
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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
    • 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
    • C02F1/48—Treatment of water, waste water, or sewage with magnetic or electric fields
    • C02F1/488—Treatment of water, waste water, or sewage with magnetic or electric fields for separation of magnetic materials, e.g. magnetic flocculation
    • 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
    • C02F1/52—Treatment of water, waste water, or sewage by flocculation or precipitation of suspended impurities
    • C02F1/5236—Treatment of water, waste water, or sewage by flocculation or precipitation of suspended impurities using inorganic agents
    • 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
    • C02F1/52—Treatment of water, waste water, or sewage by flocculation or precipitation of suspended impurities
    • C02F1/5281—Installations for water purification using chemical agents
    • 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
    • C02F2303/14—Maintenance of water treatment installations
    • 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
    • C02F3/28—Anaerobic digestion processes
    • C02F3/2826—Anaerobic digestion processes using anaerobic filters
    • 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
    • C02F3/28—Anaerobic digestion processes
    • C02F3/2866—Particular arrangements for anaerobic reactors

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  • Life Sciences & Earth Sciences (AREA)
  • Hydrology & Water Resources (AREA)
  • Engineering & Computer Science (AREA)
  • Environmental & Geological Engineering (AREA)
  • Water Supply & Treatment (AREA)
  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Water Treatment By Electricity Or Magnetism (AREA)

Abstract

The invention discloses a high-efficiency sedimentation and denitrification sewage treatment system, which comprises a high-efficiency sedimentation device and a denitrification device, wherein the high-efficiency sedimentation device comprises a quick mixing tank, a magnetic powder mixing tank, a flocculation tank and a sedimentation tank, the denitrification device comprises a water inlet well, a mixing tank and a denitrification deep bed filter tank, the water outlet of the sedimentation tank is communicated with the water inlet of the water inlet well, a filter material layer is arranged in the denitrification deep bed filter tank, the bottom of the filter material layer is provided with a bearing layer, the denitrification deep bed filter tank is also internally provided with a gas-water distribution system, the gas-water distribution system comprises a filter brick layer, the filter brick layer is positioned at the bottom of the supporting layer, the backwashing water inlet assembly is connected with the water inlet distributor, the backwashing air inlet assembly is connected with the air inlet distributor, and a water outlet of the backwashing water inlet assembly and a gas outlet of the backwashing air inlet assembly are respectively positioned at the bottom of the filter brick layer. The back washing water and the back washing gas of the denitrification filter can be uniformly distributed.

Description

High-efficient sediment and denitrification sewage treatment system
Technical Field
The invention relates to the field of sewage treatment, in particular to a high-efficiency precipitation and denitrification sewage treatment system.
Background
In the existing denitrification sewage treatment system, a filter material layer and a bearing layer positioned below the filter material layer are arranged in a denitrification filter tank, and a gas-water distribution system is generally arranged in the denitrification filter tank and generally comprises a filter brick layer, a backwashing water inlet pipe and a backwashing air inlet pipe. Although the back washing water of the back washing water inlet pipe and the gas of the back washing air inlet pipe are distributed through the filter brick layer, the back washing water and the back washing gas still have the problem of uneven distribution.
Disclosure of Invention
The invention aims to provide a high-efficiency sedimentation tank and a denitrification sewage treatment system.
The technical scheme is as follows:
a high-efficiency sedimentation and denitrification sewage treatment system comprises a high-efficiency sedimentation device and a denitrification device, wherein the high-efficiency sedimentation device comprises a rapid mixing tank, a magnetic powder mixing tank, a flocculation tank and a sedimentation tank which are sequentially communicated, the denitrification device comprises a water inlet well, a mixing tank and a denitrification deep bed filter tank which are sequentially communicated, a water outlet of the sedimentation tank is communicated with a water inlet of the water inlet well through a water conveying pipe, a filter material layer is arranged in the denitrification deep bed filter tank, a bearing layer is arranged at the bottom of the filter material layer, a gas-water distribution system is further arranged in the denitrification deep bed filter tank and comprises a filter brick layer, a backwashing water inlet assembly, a backwashing gas inlet assembly, a water inlet distributor and a gas inlet distributor, the filter brick layer is positioned at the bottom of the bearing layer, the backwashing water inlet assembly is connected with the water inlet distributor, the backwashing gas inlet assembly is connected with the gas inlet distributor, the water outlet of the backwashing water inlet assembly and the air outlet of the backwashing air inlet assembly are respectively positioned at the bottom of the filter brick layer.
The backwashing water inlet assembly comprises a water inlet main pipe and a plurality of water inlet branch pipes, the water inlet distributor is connected with the water inlet main pipe, and backwashing water enters the water inlet branch pipes after passing through the water inlet distributor; the backwashing air inlet assembly comprises an air inlet main pipe and a plurality of air inlet branch pipes, the air inlet distributor is connected with the air inlet main pipe, and backwashing air enters the air inlet branch pipes after passing through the air inlet distributor.
The water inlet distributor and the air inlet distributor at least comprise a first distribution cavity and a second distribution cavity, an inlet is formed in one end of the first distribution cavity, a through hole is formed between the first distribution cavity and the second distribution cavity, an outlet is formed in one side edge of the second distribution cavity, the diameter of the through hole is smaller than that of the inlet, and the diameter of the outlet is smaller than that of the through hole.
The water inlet well and be equipped with first breakwater between the mixed pond, the upper portion of first breakwater is equipped with first water hole of crossing, mix the pond with be equipped with second breakwater, third breakwater and fourth breakwater between the deep bed filtering pond of denitrification, the lower part of second breakwater is equipped with the second and crosses the water hole, the upper portion of third breakwater is equipped with the third and crosses the water hole, the upper portion of fourth breakwater is equipped with the fourth and crosses the water hole, the third crosses the water hole and opens and close through flashboard control.
Sedimentation tank upper portion is equipped with first swash plate subassembly and second swash plate subassembly, first swash plate subassembly includes the first swash plate of a plurality of slopes, the second swash plate subassembly include a plurality of slopes with a plurality of the second swash plate that first swash plate corresponds, first swash plate is located second swash plate top, first swash plate with the incline direction of second swash plate is opposite.
The quick mixing tank and between the magnetic mixing tank, the magnetic mixing tank and between the flocculation tank, the flocculation tank with be equipped with fifth baffle and sixth baffle between the sedimentation tank respectively, the fifth baffle with be equipped with the clearance between the sixth baffle, be equipped with the fifth hole of crossing water on the fifth baffle, be equipped with the sixth hole of crossing water on the sixth baffle.
The magnetic powder mixing device is characterized in that a mud scraper is arranged in the sedimentation tank, a sludge hopper is arranged at the bottom of the sedimentation tank, a sludge outlet is arranged at the bottom of the sludge hopper, the sludge outlet is connected with the magnetic powder mixing tank through a sludge conveying pipe, and a magnetic powder shearing machine and a magnetic powder recovery device are connected to the sludge conveying pipe.
And an ultrasonic mud level meter is arranged on the inner wall of the middle lower part of the sedimentation tank.
The filter brick layer includes a plurality of consecutive filter bricks, the relative both sides limit of filter brick is equipped with the reinforcing plate respectively, is equipped with the bulge on the reinforcing plate of one side, is equipped with the depressed part on the reinforcing plate of opposite side, the height of bulge is greater than the depressed part is adjacent the filter brick passes through the bulge reaches the depressed part links to each other.
The bottom of filter brick is equipped with two supporting legss, the bottom of supporting legs is equipped with anti-skidding portion, antiskid portion includes a plurality of convex bumps.
The following illustrates the advantages or principles of the invention:
the efficient precipitation and denitrification sewage treatment system comprises an efficient precipitation device and a denitrification sewage treatment system, when the system is used for sewage treatment, sewage firstly enters a fast mixing tank of the efficient precipitation device, a liquid aluminum chloride coagulant aid is added into the fast mixing tank, a fast mixing stirrer is arranged in the fast mixing tank, and the sewage and the coagulant aid are rapidly mixed through stirring and then enter a magnetic powder mixing tank. And adding magnetic powder into the magnetic powder mixing tank, and stirring and mixing the magnetic powder and the sewage to enter the flocculation tank. And adding a flocculating agent into the flocculation tank, and allowing the sewage and the flocculating agent to enter the sedimentation tank after flocculation reaction. The magnetic powder and the sludge are settled at the bottom of the sedimentation tank and are subjected to gravity concentration, and the clear water enters a water inlet well of the denitrification device through a water delivery pipe. Clear water enters a mixing tank after passing through a water inlet well, sodium acetate is added into the mixing tank, the clear water and the sodium acetate react and then enter a denitrification filter tank, and the clear water is discharged after passing through a filter material layer, a bearing layer and a filter brick layer.
The invention needs to carry out back washing on the filter material layer and the supporting layer, the back washing entering assembly firstly carries out water distribution through the water inlet distributor and then carries out secondary distribution on water through the filter brick layer, thereby ensuring that the water pressure of the back washing water is uniformly distributed. The backwash gas inlet assembly firstly distributes gas through the gas inlet distributor and then secondarily distributes the gas through the filter brick layer, so that the uniform distribution of the gas pressure of the backwash gas is guaranteed.
Drawings
FIG. 1 is a schematic structural diagram of a high-efficiency precipitation apparatus of the present embodiment;
FIG. 2 is a first sectional view of the denitrification apparatus of the present embodiment;
FIG. 3 is a second sectional view of the denitrification apparatus of the present embodiment;
FIG. 4 is a third sectional view of the denitrification apparatus of the present embodiment; (ii) a
FIG. 5 is a schematic view of the structure of the water inlet distributor of the present embodiment;
FIG. 6 is a schematic view showing the construction of the filter block of the present embodiment;
description of reference numerals:
10. a fast mixing tank; 20. a magnetic powder mixing tank; 30. a flocculation tank; 40. a sedimentation tank; 50. a fifth baffle; 60. a sixth baffle; 51. a fifth water passing hole; 61. a sixth water passing hole; 70. a first sloping plate; 80. a second swash plate; 90. an effluent weir; 100. a mud scraper; 110. a sludge hopper; 120. a magnetic powder shearing machine; 130. a magnetic powder recovery device; 140. an ultrasonic mud level meter; 150. clear water is discharged from the water collecting channel; 160. a water inlet well; 170. a mixing tank; 180. a denitrification deep bed filter; 190. a first water baffle; 191. a first water passing hole; 200. a second water baffle; 210. a third water baffle; 220. a fourth water baffle; 201. a second water passing hole; 211. a third water passing hole; 221. a fourth water passing hole; 230. a filter material layer; 240. a support layer; 250. a brick filtering layer; 260. a water inlet distributor; 270. an intake air distributor; 280. a main water inlet pipe; 290. a water inlet branch pipe; 300. a main air inlet pipe; 310. an intake branch pipe; 261. a first distribution chamber; 262. a second distribution chamber; 263. an inlet; 264. a through hole; 265. an outlet; 251. filtering bricks; 2511. a reinforcing plate; 2512. a projection; 2513. a recessed portion; 2514. supporting legs; 2515. and an anti-slip part.
Detailed Description
In the description of the present invention, it is to be understood that the terms "upper", "lower", "front", "rear", "left", "right", "vertical", "horizontal", "middle", "inner", and the like indicate orientations or positional relationships based on those shown in the drawings, and are only for convenience of description and simplicity of description, but do not indicate or imply that the referred device or element must have a specific orientation, be constructed in a specific orientation, and be operated, and thus, should not be construed as limiting the present invention. Furthermore, the terms "first", "second", etc. are used for descriptive purposes only and are not to be construed as indicating or implying relative importance or implicitly indicating the number of technical features indicated. Thus, a feature defined as "first," "second," etc. may explicitly or implicitly include one or more of that feature. In the description of the present invention, it should be noted that, unless otherwise explicitly specified or limited, the terms "mounted," "connected," and "connected" are to be construed broadly, e.g., as meaning either a fixed connection, a removable connection, or an integral connection; they may be connected directly or indirectly through intervening media, or they may be interconnected between two elements. The specific meaning of the above terms in the present invention can be understood by those of ordinary skill in the art through specific situations.
The following detailed description of the preferred embodiments of the present invention, taken in conjunction with the accompanying drawings, will make the advantages and features of the invention easier to understand by those skilled in the art, and thus will clearly and clearly define the scope of the invention.
As shown in fig. 1 to 6, the present embodiment discloses a high efficiency sedimentation and denitrification sewage treatment system, which comprises a high efficiency sedimentation device and a denitrification device, wherein the high efficiency sedimentation device is communicated with the denitrification device. The high-efficiency sedimentation device comprises a quick mixing tank 10, a magnetic powder mixing tank 20, a flocculation tank 30 and a sedimentation tank 40 which are sequentially communicated. Wherein, all be fixed with the mixer in mixing pond 10, the magnetic mixing pond 20 and the flocculation basin 30 soon, mix between pond 10 and the magnetic mixing pond 20 soon, between magnetic mixing pond 20 and the flocculation basin 30, be equipped with fifth baffle 50 and sixth baffle 60 between flocculation basin 30 and the sedimentation tank 40 respectively, be equipped with the clearance between fifth baffle 50 and the sixth baffle 60, be equipped with the fifth hole 51 of crossing water on the fifth baffle 50, be equipped with the sixth hole 61 of crossing water on the sixth baffle 60.
The upper portion of the sedimentation tank 40 is provided with a first inclined plate component and a second inclined plate component, the first inclined plate component comprises a plurality of inclined first inclined plates 70, the second inclined plate component comprises a plurality of inclined second inclined plates 80 corresponding to the first inclined plates 70, the first inclined plates 70 are positioned above the second inclined plates 80, and the inclined directions of the first inclined plates 70 and the second inclined plates 80 are opposite. A plurality of U-shaped effluent weirs 90 are arranged above the first inclined plate component.
A mud scraper 100 is arranged in the sedimentation tank 40, a sludge hopper 110 is arranged at the bottom of the sedimentation tank 40, a sludge outlet is arranged at the bottom of the sludge hopper 110, the sludge outlet is connected with the magnetic powder mixing tank 20 through a sludge conveying pipe, and a magnetic powder shearing machine 120 and a magnetic powder recovery device 130 are connected to the sludge conveying pipe.
The sewage is firstly conveyed to the quick mixing tank 10 through a conveying pipe, the liquid polyaluminium chloride coagulant aid is added into the quick mixing tank 10 after the sewage enters the quick mixing tank 10, and the sewage and the coagulant aid are quickly mixed through stirring. The mixed sewage enters the magnetic powder mixing tank 20 through the fifth water passing hole 51 and the sixth water passing hole 61, then the magnetic powder is added into the magnetic powder mixing tank 20, and the magnetic powder and the sewage are fully mixed after being stirred. Then the sewage in the magnetic powder mixing tank 20 enters a flocculation tank 30, then a flocculating agent is added into the flocculation tank 30, the sewage and the flocculating agent are fully reacted after stirring, and then the sewage and the sludge after reaction enter a sedimentation tank 40.
The magnetic powder and the sludge are settled at the bottom of the sedimentation tank 40 and are subjected to gravity concentration, the settled sludge is scraped and collected into a sludge hopper 110 by a sludge scraper 100, the sludge in the sludge hopper 110 can be pumped out by a magnetic reflux pump and is conveyed to a magnetic sludge shearing machine and a magnetic powder recovery device 130 through a sludge conveying pipe, and the sludge is stripped and the magnetic powder is recovered. The recovered magnetic powder enters the magnetic powder mixing tank 20 again to continue to participate in the reaction, and the sludge enters a subsequent sludge treatment system. The magnetic powder recovery device 130 of the present embodiment is a magnetic powder recovery device used in the existing sewage treatment.
The inner wall of the middle lower part of the sedimentation tank 40 is also provided with an ultrasonic mud level meter 140. The ultrasonic sludge level gauge 140 is used to detect the sludge level in the sedimentation tank 40. When the amount of sludge in the sedimentation tank 40 is large and the sludge in the sedimentation tank 40 reaches a certain height, the sludge can be directly conveyed to a subsequent sludge treatment system through the sludge conveying pipe.
The sewage in the sedimentation tank 40 passes through the first inclined plate 70 and the second inclined plate 80, then flows to the effluent weir 90, and is collected to the clear water effluent collecting channel 150 through the effluent weir 90 to be converged. The lighter particles in the sewage are intercepted on the inclined plate. When the sludge on the inclined plate is accumulated to a certain degree, the sludge can automatically slide down. Because the first inclined plate 70 and the second inclined plate 80 are arranged in the embodiment, after the sewage passes through the first inclined plate 70 and the second inclined plate 80, particles in the sewage are intercepted, the water quality of the water entering the effluent weir 90 is light, and the treatment effect is good.
The clear water outlet collecting channel 150 is connected with the denitrification device through a conveying pipe. As shown in FIG. 2, the denitrification apparatus of the present embodiment comprises a water inlet well 160, a mixing tank 170 and a denitrification deep-bed filter 180 which are communicated in sequence. The water outlet of the clear water outlet collecting channel 150 is communicated with the water inlet of the water inlet well 160 through a water conveying pipe, a first water baffle 190 is arranged between the water inlet well 160 and the mixing pool 170, a first water passing hole 191 is formed in the upper portion of the first water baffle 190, a second water baffle 200 is arranged between the mixing pool 170 and the denitrification deep bed filter 180, a third water baffle 210 and a fourth water baffle 220 are arranged, a second water passing hole 201 is formed in the lower portion of the second water baffle 200, a third water passing hole 211 is formed in the upper portion of the third water baffle 210, a fourth water passing hole 221 is formed in the upper portion of the fourth water baffle 220, and the third water passing hole 211 is controlled to be opened and closed through a gate plate.
The denitrification deep bed filter 180 is internally provided with a filter material layer 230, the filter material layer 230 is a quartz sand filter material, the height of the filter material layer 230 is 1.8-1.9m, denitrifying bacteria are attached to and grow on the surface of the filter material layer 230 in the embodiment, the bottom of the filter material layer 230 is provided with a supporting layer 240, the supporting layer 240 is distributed by adopting five grades of cobblestones, and the thickness of the supporting layer 240 is about 450 mm. The denitrification deep bed filter 180 is also internally provided with a gas-water distribution system, the gas-water distribution system comprises a filter brick layer 250, a backwashing water inlet assembly, a backwashing gas inlet assembly, a water inlet distributor 260 and a gas inlet distributor 270, the filter brick layer 250 is positioned at the bottom of the supporting layer 240, the backwashing water inlet assembly is connected with the water inlet distributor 260, the backwashing gas inlet assembly is connected with the gas inlet distributor 270, and a water outlet of the backwashing water inlet assembly and a gas outlet of the backwashing gas inlet assembly are respectively positioned at the bottom of the filter brick layer 250. The bottom of the filter brick layer 250 is provided with a drainage channel.
The backwashing water inlet assembly comprises a main water inlet pipe 280 and a plurality of water inlet branch pipes 290, wherein the water inlet distributor 260 is connected with the main water inlet pipe 280, and backwashing water enters the water inlet branch pipes 290 after passing through the water inlet distributor 260; the backwash gas inlet assembly comprises a main gas inlet pipe 300 and a plurality of branch gas inlet pipes 310, wherein the gas inlet distributor 270 is connected with the main gas inlet pipe 300, and backwash gas enters the branch gas inlet pipes 310 after passing through the gas inlet distributor 270.
The water inlet distributor 260 and the air inlet distributor 270 each include at least a first distribution cavity 261 and a second distribution cavity 262, an inlet 263 is disposed at one end of the first distribution cavity 261, a through hole 264 is disposed between the first distribution cavity 261 and the second distribution cavity 262, an outlet 265 is disposed at one side of the second distribution cavity 262, a diameter of the through hole 264 is smaller than a diameter of the inlet 263, and a diameter of the outlet 265 is smaller than a diameter of the through hole 264.
The filter brick layer 250 comprises a plurality of filter bricks 251 which are connected in sequence, reinforcing plates 2511 are respectively arranged on two opposite side edges of the filter bricks 251, a convex portion 2512 is arranged on the reinforcing plate 2511 on one side, a concave portion 2513 is arranged on the reinforcing plate 2511 on the other side, the height of the convex portion 2512 is larger than that of the concave portion 2513, and the adjacent filter bricks 251 are connected through the convex portion 2512 and the concave portion 2513. Two supporting legs 2514 are arranged at the bottom of the filter brick 251, an anti-slip part 2515 is arranged at the bottom of the supporting legs 2514, and the anti-slip part 2515 comprises a plurality of convex points.
Clear water enters the water inlet well 160 and is conveyed to the mixing tank 170 through the first water passing hole 191, sodium acetate is added into the mixing tank 170, the clear water and the sodium acetate enter the denitrification filter tank after being stirred and reacted, and then the clear water enters the drainage channel after passing through the filter material layer 230, the supporting layer 240 and the filter brick layer 250 and is discharged.
When the filter material layer 230 needs to be backwashed, the backwashing can be carried out through the backwashing water inlet assembly and the backwashing air inlet assembly. Cleaning water of the backwashing water inlet assembly firstly enters the water inlet main pipe 280, then enters the first distribution cavity 261 of the water inlet distributor 260 to be mixed, then enters the second distribution cavity 262 to be mixed, then continuously enters each water inlet branch pipe 290 through the main water inlet pipe, and enters the supporting layer 240 and the filter material layer 230 to be backwashed after passing through the filter brick layer 250 through the spray head of each water inlet branch pipe 290. The cleaned cleaning water can be collected by the cleaning water collecting channel and then discharged. Similarly, the backwash gas of the backwash gas inlet assembly firstly enters the main gas inlet pipe 300, then enters the first distribution cavity 261 of the gas inlet distributor 270 for mixing, then enters the second distribution cavity 262 for mixing, then continues to enter each gas inlet branch pipe 310 through the main gas inlet pipe 300, and enters the support layer 240 and the filter material layer 230 through the nozzles of each gas inlet branch pipe 310 after passing through the filter brick layer 250 for backwash.
The embodiments of the present invention are not limited thereto, and according to the above-mentioned contents of the present invention, the present invention can be modified, substituted or combined in other various forms without departing from the basic technical idea of the present invention.

Claims (10)

1. A high-efficiency sedimentation and denitrification sewage treatment system is characterized by comprising a high-efficiency sedimentation device and a denitrification device, wherein the high-efficiency sedimentation device comprises a rapid mixing tank, a magnetic powder mixing tank, a flocculation tank and a sedimentation tank which are sequentially communicated, the denitrification device comprises a water inlet well, a mixing tank and a denitrification deep bed filter tank which are sequentially communicated, a water outlet of the sedimentation tank is communicated with a water inlet of the water inlet well through a water conveying pipe, a filter material layer is arranged in the denitrification deep bed filter tank, a bearing layer is arranged at the bottom of the filter material layer, a gas-water distribution system is further arranged in the denitrification deep bed filter tank and comprises a filter brick layer, a backwashing water inlet component, a backwashing gas inlet component, a water inlet distributor and a gas inlet distributor, the filter brick layer is positioned at the bottom of the bearing layer, and the backwashing water inlet component is connected with the backwashing water inlet distributor, the backwashing air inlet assembly is connected with the air inlet distributor, and the water outlet of the backwashing water inlet assembly and the air outlet of the backwashing air inlet assembly are respectively positioned at the bottom of the filter brick layer.
2. The high efficiency settling and denitrification sewage treatment system as claimed in claim 1, wherein the backwash water inlet assembly comprises a main water inlet pipe and a plurality of water inlet branch pipes, the water inlet distributor is connected with the main water inlet pipe, and backwash water enters the water inlet branch pipes after passing through the water inlet distributor; the backwashing air inlet assembly comprises an air inlet main pipe and a plurality of air inlet branch pipes, the air inlet distributor is connected with the air inlet main pipe, and backwashing air enters the air inlet branch pipes after passing through the air inlet distributor.
3. The high efficiency settling and denitrification sewage treatment system as claimed in claim 2, wherein the influent distributor and the influent distributor each comprise at least a first distribution chamber and a second distribution chamber, the first distribution chamber has an inlet at one end, a through hole is formed between the first distribution chamber and the second distribution chamber, the second distribution chamber has an outlet at one side, the diameter of the through hole is smaller than that of the inlet, and the diameter of the outlet is smaller than that of the through hole.
4. The high efficiency sedimentation and denitrification sewage treatment system according to claim 1, wherein a first water baffle is arranged between the water inlet well and the mixing tank, a first water passing hole is formed in the upper portion of the first water baffle, a second water baffle, a third water baffle and a fourth water baffle are arranged between the mixing tank and the denitrification deep bed filter, a second water passing hole is formed in the lower portion of the second water baffle, a third water passing hole is formed in the upper portion of the third water baffle, a fourth water passing hole is formed in the upper portion of the fourth water baffle, and the opening and closing of the third water passing hole are controlled by a gate plate.
5. The high efficiency sedimentation and denitrification sewage treatment system according to any one of claims 1 to 4, wherein a first inclined plate assembly and a second inclined plate assembly are provided at an upper portion of the sedimentation tank, the first inclined plate assembly comprises a plurality of inclined first inclined plates, the second inclined plate assembly comprises a plurality of inclined second inclined plates corresponding to the plurality of first inclined plates, the first inclined plates are located above the second inclined plates, and the inclination directions of the first inclined plates and the second inclined plates are opposite.
6. The sewage treatment system with high efficiency sedimentation and denitrification according to claim 1, wherein a fifth baffle and a sixth baffle are respectively arranged between the rapid mixing tank and the magnetic powder mixing tank and between the magnetic powder mixing tank and the flocculation tank, a gap is arranged between the fifth baffle and the sixth baffle, a fifth water passing hole is arranged on the fifth baffle, and a sixth water passing hole is arranged on the sixth baffle.
7. The high efficiency sewage treatment system of claim 1, wherein a sludge scraper is arranged in the sedimentation tank, a sludge hopper is arranged at the bottom of the sedimentation tank, a sludge outlet is arranged at the bottom of the sludge hopper, the sludge outlet is connected with the magnetic powder mixing tank through a sludge conveying pipe, and a magnetic powder shearing machine and a magnetic powder recovery device are connected to the sludge conveying pipe.
8. The high efficiency sedimentation and denitrification sewage treatment system according to claim 1, wherein an ultrasonic mud level meter is arranged on the inner wall of the middle lower part of the sedimentation tank.
9. The high efficiency settling and denitrification sewage treatment system according to claim 1, wherein the filter brick layer comprises a plurality of filter bricks connected in series, wherein the opposite sides of the filter bricks are respectively provided with a reinforcing plate, the reinforcing plate on one side is provided with a convex portion, the reinforcing plate on the other side is provided with a concave portion, the height of the convex portion is greater than that of the concave portion, and the adjacent filter bricks are connected through the convex portion and the concave portion.
10. The high efficiency settling and denitrification sewage treatment system according to claim 9 wherein the bottom of the filter brick is provided with two support feet, the bottom of the support feet are provided with anti-slip portions, and the anti-slip portions comprise a plurality of raised bumps.
CN202011180663.8A 2020-10-29 2020-10-29 High-efficient sediment and denitrification sewage treatment system Pending CN112321077A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN202011180663.8A CN112321077A (en) 2020-10-29 2020-10-29 High-efficient sediment and denitrification sewage treatment system

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN202011180663.8A CN112321077A (en) 2020-10-29 2020-10-29 High-efficient sediment and denitrification sewage treatment system

Publications (1)

Publication Number Publication Date
CN112321077A true CN112321077A (en) 2021-02-05

Family

ID=74296392

Family Applications (1)

Application Number Title Priority Date Filing Date
CN202011180663.8A Pending CN112321077A (en) 2020-10-29 2020-10-29 High-efficient sediment and denitrification sewage treatment system

Country Status (1)

Country Link
CN (1) CN112321077A (en)

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