Modular three-phase separation precipitator

Through the modularly designed three-phase separation precipitator, the gas-liquid solid separation efficiency and solid cut-off rate in sewage treatment are improved through structures such as inclined pipe sedimentation zone and baffle plate, and the low separation efficiency and structure in the prior art are solved. The problem of inflexibility achieves efficient sewage treatment and low-cost maintenance.

CN222218706UActive Publication Date: 2024-12-24WUHAN FUND ENVIRONMENT PROTECTION
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Patent Information

Application Number
CN202420877144.4
Authority / Receiving Office
CN · China
Patent Type
Utility models(China)
Current Assignee / Owner
Filing Date
2024-04-25
Publication Date
2024-12-24
Estimated Expiration
2034-04-25

AI Technical Summary

Technical Problem

The existing three-phase separators have low separation efficiency and solid cut-off rate in sewage treatment, and the structure is difficult to adjust flexibly, which wastes space and high maintenance costs.

Method used

The three-phase separation precipitator adopts a modular design, consisting of multiple three-phase separation monomers closely fixed together, including an inclined tube precipitation area, a baffle plate, an overflow hole and an expanded tube port to achieve gas-liquid-solid separation. And the three-phase separation monomers are bolted to form a matrix distribution.

Benefits of technology

It improves installation efficiency and maintenance costs, improves gas-liquid-solid separation efficiency and solid cut-off rate, optimizes the effluent water quality, and can flexibly replace monomers to adapt to changes in the biological reaction zone.

✦ Generated by Eureka AI based on patent content.

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Abstract

The utility model discloses a modular three-phase separation precipitator which comprises an inclined tube precipitation area and a plurality of three-phase separation single bodies, an effluent weir is arranged on the upper edge of the inner side of the inclined tube precipitation area, the three-phase separation single bodies are tightly fixed together to form a three-phase separation area, the three-phase separation area is located under the inclined tube precipitation area, and the three-phase separation single bodies are arranged in the inclined tube precipitation area. The bottom edge of the inclined tube settling zone abuts against the outer edge of the three-phase separation zone, the inner side, close to the bottom edge, of the side wall of the inclined tube settling zone is bent inwards to form a baffle plate, the baffle plate is provided with an overflowing hole right opposite to the three-phase separation single body, and the three-phase separation single body is of a hopper-shaped structure with an upper opening and a lower opening. The three-phase separation precipitator adopts a modular design, is formed by assembling a plurality of three-phase separator monomers, and is high in installation efficiency, low in installation cost and later maintenance cost, high in equipment gas collection efficiency and solid interception rate and good in effluent quality.
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Description

Technical Field

[0001] The utility model relates to the technical field of sewage treatment, in particular to a modular three-phase separation precipitator. Background Art

[0002] The three-phase separator is mainly used in the biological treatment stage of sewage treatment, which can effectively separate the three phases of gas, liquid and solid. There are many types of three-phase separators with different structures, but they all have the disadvantages of low separation efficiency and solid interception rate. In addition, the three-phase separators mostly adopt civil engineering structures, with useless space at the bottom, wasting tank capacity, and it is difficult to flexibly change according to the conditions of the biological reaction area. Utility Model Content

[0003] In view of the above technical problems, the utility model proposes a modular three-phase separation precipitator. The three-phase separation precipitator adopts a modular design and is assembled from multiple three-phase separator monomers. It has high installation efficiency, low installation cost and subsequent maintenance cost, high equipment gas collection efficiency and solid interception rate, and good effluent water quality.

[0004] A modular three-phase separation sedimentation device comprises an inclined tube sedimentation zone, an inner upper edge of which is provided with a water outlet weir, and a plurality of three-phase separation monomers. A plurality of the three-phase separation monomers are tightly fixed together to form a three-phase separation zone, wherein the three-phase separation zone is located directly below the inclined tube sedimentation zone, the bottom edge of the inclined tube sedimentation zone abuts against the outer edge of the three-phase separation zone, the inner side of the side wall of the inclined tube sedimentation zone is bent inwards near the bottom edge to form a baffle, the baffle is provided with a flow hole directly opposite to the three-phase separation monomer, and the three-phase separation monomer is a bucket-shaped structure with upper and lower openings.

[0005] As a preferred embodiment of the above technical solution, the three-phase separation monomer includes a first side plate, a second side plate, an air baffle plate and a sliding mud ramp plate, which enclose a bucket-shaped structure with upper and lower openings, and the sliding mud ramp plate is arranged opposite to the air baffle plate, and the sliding mud ramp plate protrudes downward from the outlet of the bucket-shaped structure, and the end of the air baffle plate is folded outward to form a pipe mouth extension plate, and the pipe mouth extension plate and the sliding mud ramp plate form an expanded pipe mouth below the outlet of the bucket-shaped structure, and the sliding mud ramp plate and the air baffle plate located on both sides of the three-phase separation zone are bent vertically upward to form a guide plate.

[0006] As a preferred embodiment of the above technical solution, the upper edge of the guide plate is higher than the upper edge of the baffle.

[0007] As a preferred embodiment of the above technical solution, two adjacent three-phase separation monomers are fixedly connected by bolts.

[0008] As a preferred embodiment of the above technical solution, the plurality of three-phase separation monomers are evenly distributed in a matrix.

[0009] The beneficial effects of the utility model are:

[0010] 1. It adopts modular design and is assembled from multiple three-phase separator monomers. It has high installation efficiency and low cost. The blocked three-phase separator monomer can be replaced separately, which is convenient for later maintenance.

[0011] 2. The gas-liquid-solid three-phase separation efficiency is high, the equipment has high gas collection efficiency and solid interception rate, and the effluent water quality is good.

[0012] 3. The expansion nozzle design for water and mud separation in the three-phase separator enables fast mud discharge. BRIEF DESCRIPTION OF THE DRAWINGS

[0013] Figure 1 It is a top view of the three-phase separation zone of the utility model.

[0014] Figure 2 for Figure 1 Middle AA section view (section view of the overall structural schematic).

[0015] Figure 3 for Figure 1 Middle BB section view (section view of the overall structural schematic).

[0016] The figure numbers are as follows: 1- inclined tube sedimentation zone, 2- outlet weir, 3- three-phase separation monomer, 4- three-phase separation zone, 5- baffle, 6- flow hole, 7- first side plate, 8- second side plate, 9- air baffle, 10- mud inclined plate, 11- pipe mouth expansion plate, 12- expansion pipe mouth, 13- guide plate. DETAILED DESCRIPTION

[0017] The following is a clear and complete description of the technical solution of the utility model in conjunction with the accompanying drawings of the utility model. Based on the embodiments of the utility model, all other embodiments obtained by ordinary technicians in this field without creative work are within the scope of protection of the utility model.

[0018] like Figures 1 to 3 A modular three-phase separation sedimentation tank is shown, comprising an inclined tube sedimentation zone 1, an inner upper edge of which is provided with a water outlet weir 2, and a plurality of three-phase separation monomers 3, wherein the plurality of three-phase separation monomers 3 are tightly fixed together to form a three-phase separation zone 4, wherein the three-phase separation zone 4 is located directly below the inclined tube sedimentation zone 1, wherein the bottom edge of the inclined tube sedimentation zone 1 abuts against the outer edge of the three-phase separation zone 4, and the inner side of the side wall of the inclined tube sedimentation zone 1 is bent inwardly near the bottom edge to form a baffle 5, wherein the baffle 5 has a flow hole 6 directly opposite to the three-phase separation monomer 3, and the three-phase separation monomer 3 is a bucket-shaped structure with upper and lower openings.

[0019] In this embodiment, the three-phase separation monomer 3 includes a first side plate 7, a second side plate 8, an air baffle plate 9 and a sliding mud ramp plate 10. The first side plate 7, the second side plate 8, the air baffle plate 9 and the sliding mud ramp plate 10 enclose a bucket-shaped structure with upper and lower openings. The sliding mud ramp plate 10 is arranged opposite to the air baffle plate 9. The sliding mud ramp plate 10 protrudes downward from the outlet of the bucket-shaped structure. The end of the air baffle plate 9 is folded outward to form a pipe mouth expansion plate 11. The pipe mouth expansion plate 11 and the sliding mud ramp plate 10 form an expansion pipe mouth 12 below the outlet of the bucket-shaped structure. The sliding mud ramp plates 10 and the air baffle plates 9 located on both sides of the three-phase separation zone 4 are bent vertically upward to form a guide plate 13.

[0020] In this embodiment, the upper edge of the guide plate 13 is higher than the upper edge of the baffle plate 5 .

[0021] In this embodiment, two adjacent three-phase separation units 3 are fixedly connected by bolts.

[0022] In this embodiment, the plurality of three-phase separation units 3 are evenly distributed in a matrix.

[0023] The working principle of this embodiment is as follows.

[0024] Water passes through the bottom of the three-phase separator, and the inverted V-shaped angle formed by the air baffle 9 and the sliding mud ramp 10 blocks the flow and stabilizes the flow. The tiny bubbles in the reaction zone form larger bubbles during the rising process. The bubbles move along the inverted V-shaped angle formed by the air baffle 9 and the sliding mud ramp 10 and are discharged from the V-shaped channel formed by the bucket-shaped module to the reaction zone, realizing gas-liquid separation. The wastewater enters the three-phase separation zone through the flow guide plates 13 on both sides of the modular three-phase separation precipitator through the flow hole 6. After the liquid enters, it passes through the baffle 5, and the gas gathers upward and then returns to the reaction zone to realize gas-liquid separation. In the three-phase separator, due to the high specific gravity of the sludge, the sludge passes downward through the expansion nozzle 12 and slides into the bottom along the sliding mud ramp 10 to realize mud-liquid separation. The separated liquid continues to rise, and the suspended particles are once again intercepted and precipitated into the three-phase separation zone through the inclined tube sedimentation zone. The separated water is discharged through the outlet weir to meet the standards, and finally realizes the efficient separation of mud, gas and water.

[0025] The above are only preferred embodiments of the present invention and are not intended to limit the present invention. For those skilled in the art, the present invention may be subject to various modifications and variations. Any modification, equivalent replacement, improvement, etc. made within the spirit and principle of the present invention shall be included in the protection scope of the present invention.

Claims

1. A modular three-phase separation precipitator, comprising an inclined tube sedimentation zone, wherein an outlet weir is provided on the inner upper edge of the inclined tube sedimentation zone, and characterized in that: It includes a plurality of three-phase separation monomers, and a plurality of the three-phase separation monomers are tightly fixed together to form a three-phase separation zone, wherein the three-phase separation zone is located directly below the inclined tube sedimentation zone, and the bottom edge of the inclined tube sedimentation zone abuts against the outer edge of the three-phase separation zone, and the inner side of the side wall of the inclined tube sedimentation zone is bent inward near the bottom edge to form a baffle, and the baffle is provided with a flow hole directly opposite to the three-phase separation monomer, and the three-phase separation monomer is a bucket-shaped structure with upper and lower openings.

2. The modular three-phase separation precipitator according to claim 1, characterized in that: The three-phase separation monomer includes a first side plate, a second side plate, an air baffle plate and a sliding mud ramp plate. The first side plate, the second side plate, the air baffle plate and the sliding mud ramp plate are enclosed to form a bucket-shaped structure with upper and lower openings. The sliding mud ramp plate is arranged opposite to the air baffle plate. The sliding mud ramp plate protrudes downward from the outlet of the bucket-shaped structure. The end of the air baffle plate is folded outward to form a pipe mouth expansion plate. The pipe mouth expansion plate and the sliding mud ramp plate form an expanded pipe mouth below the outlet of the bucket-shaped structure. The sliding mud ramp plates and the air baffle plates located on both sides of the three-phase separation zone are bent vertically upward to form a guide plate.

3. The modular three-phase separation precipitator according to claim 2, characterized in that: The upper edge of the guide plate is higher than the upper edge of the baffle plate.

4. The modular three-phase separation precipitator according to claim 1, characterized in that: Two adjacent three-phase separation monomers are fixedly connected by bolts.

5. The modular three-phase separation precipitator according to claim 1, characterized in that: The plurality of three-phase separation monomers are evenly distributed in a matrix.