CN220502793U - Ozone flow distributor for advanced oxidation reaction of sewage treatment - Google Patents
Ozone flow distributor for advanced oxidation reaction of sewage treatment Download PDFInfo
- Publication number
- CN220502793U CN220502793U CN202321931939.0U CN202321931939U CN220502793U CN 220502793 U CN220502793 U CN 220502793U CN 202321931939 U CN202321931939 U CN 202321931939U CN 220502793 U CN220502793 U CN 220502793U
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- Prior art keywords
- pipeline
- frame
- gas
- main air
- air inlet
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- CBENFWSGALASAD-UHFFFAOYSA-N Ozone Chemical compound [O-][O+]=O CBENFWSGALASAD-UHFFFAOYSA-N 0.000 title claims abstract description 33
- 238000007254 oxidation reaction Methods 0.000 title claims abstract description 18
- 239000010865 sewage Substances 0.000 title claims abstract description 15
- 230000001105 regulatory effect Effects 0.000 claims abstract description 17
- 230000003647 oxidation Effects 0.000 claims description 6
- 230000003014 reinforcing effect Effects 0.000 claims description 4
- 238000005273 aeration Methods 0.000 abstract description 5
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 abstract description 5
- 230000000903 blocking effect Effects 0.000 abstract description 3
- 238000005452 bending Methods 0.000 abstract 1
- 238000006243 chemical reaction Methods 0.000 description 11
- 238000000034 method Methods 0.000 description 11
- 230000004048 modification Effects 0.000 description 2
- 238000012986 modification Methods 0.000 description 2
- 230000009286 beneficial effect Effects 0.000 description 1
- 238000005260 corrosion Methods 0.000 description 1
- 238000005238 degreasing Methods 0.000 description 1
- 231100000086 high toxicity Toxicity 0.000 description 1
- 239000010842 industrial wastewater Substances 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 239000002957 persistent organic pollutant Substances 0.000 description 1
- 238000013032 photocatalytic reaction Methods 0.000 description 1
- 238000004088 simulation Methods 0.000 description 1
- 239000002351 wastewater Substances 0.000 description 1
Landscapes
- Treatment Of Water By Oxidation Or Reduction (AREA)
Abstract
The utility model relates to an ozone flow distributor for advanced oxidation reaction of sewage treatment, which comprises an integral skid-mounted frame, wherein the integral skid-mounted frame comprises a bottom frame and a vertical frame, a main air inlet pipeline is arranged on the front side of the vertical frame through a plurality of pipeline supporting frames, one end of the main air inlet pipeline is provided with a main air inlet, the other end of the main air inlet pipeline is provided with a blind plate, a plurality of vertically distributed branch gas pipelines are arranged on the front side of the vertical frame through pipeline fixing clamps, a gas regulating valve, a rotameter and a meter valve are sequentially arranged on each branch gas pipeline from bottom to top, a pressure gauge is arranged on the meter valve, and the top of each branch gas pipeline is provided with an air outlet in a bending manner. The utility model has the advantages that the gas is introduced through the main gas inlet pipeline, the flow is regulated through the gas regulating valves of the branch gas pipelines of each stage, meanwhile, the blocking of the tail end pipeline or the leakage of the gas can be prevented through the display of the pressure gauge, the uniform and accurate ozone addition is ensured, the uniform aeration of the tail end is ensured, and the efficient mixing of the ozone in water is realized.
Description
Technical Field
The utility model relates to the technical field of gas flow distribution devices, in particular to an ozone flow distributor for advanced oxidation reaction of sewage treatment.
Background
With the development of modern industry, sewage treatment is more and more important. The industrial wastewater belongs to high-concentration and refractory organic wastewater, has the characteristics of high concentration of organic pollutants, complex components, poor biodegradability, serious pollution, high toxicity and the like, and is difficult to meet the treatment and reach the emission requirements by adopting conventional process equipment.
At present, most treatment processes adopt advanced oxidation treatment process through three-stage UV/O 3 /H 2 O 2 And (3) carrying out photocatalytic reaction to meet the emission treatment requirement. Ozone addition is needed at each stage of the advanced oxidation treatment process, but the problem to be solved is how to ensure uniform and accurate ozone addition in each stage of reaction zone, uniform aeration at the tail end and high-efficiency mixing of ozone in water in the use process.
Disclosure of Invention
The utility model aims to distribute the flow of ozone at each stage of advanced oxidation treatment process, and provides an ozone flow distributor for advanced oxidation reaction of sewage treatment.
The utility model adopts the following technical scheme to realize the aim:
the utility model provides an ozone flow distributor for sewage treatment advanced oxidation, including whole sled dress frame, whole sled dress frame includes chassis and erects the frame, and chassis, erects the frame and become the T shape and arrange, installs main air intake duct through a plurality of pipeline support frame on erecting the frame front side, and main air intake duct one end is equipped with main air inlet and installs the blind plate in addition one end, erects the frame front side and installs the branch gas pipeline of a plurality of vertical distribution through the pipeline fixing clip, all is equipped with gas regulating valve, rotameter and table valve on every branch gas pipeline from bottom to top in proper order, installs the manometer on the table valve, and every branch gas pipeline top all bends and is equipped with the gas outlet.
The beneficial effects of the utility model are as follows: the integrated skid-mounted distributor is used as a set of integrated skid-mounted distributor, gas is introduced through the main gas inlet pipeline, the flow is regulated through the gas regulating valve of each level of branch gas pipeline, each level of flow display is realized through observing the rotameter, meanwhile, the blocking of the tail end pipeline or the leakage of gas can be prevented through the display of the pressure gauge, the ozone pipeline of each reaction area is connected to the gas outlet through the flange, the gas enters each reaction area, the ozone addition of each reaction area is participated, the uniform and accurate ozone addition is ensured, the uniform aeration of the tail end is ensured, and the efficient mixing of ozone in water is realized.
Drawings
FIG. 1 is a front view of the present utility model;
FIG. 2 is a top view of the present utility model;
FIG. 3 is a perspective view of the present utility model;
in the figure: 1-an integral skid-mounted frame; 2-a pipeline support frame; 3-a main air intake duct; 4-a primary air inlet; 5-blind plates; 6-a pipeline fixing clip; 7-branch gas pipes; 8-a gas regulating valve; 9-rotameter; 10-meter valve; 11-a pressure gauge; 12-an air outlet;
101-a chassis; 102-a vertical frame; 103-reinforcing diagonal bracing; a 104-L shaped mounting plate; 105-mounting holes;
201-a support frame; 202-supporting columns; 203-n-shaped pipe clamp; 204-fixing the ear plate;
601-semicircular pipe clamp; 602-connecting an ear plate; 603-connecting rods;
the embodiments of the present utility model will be described in detail below with reference to the accompanying drawings.
Detailed Description
The principles and features of the present utility model are described below with reference to the drawings, the examples are illustrated for the purpose of illustrating the utility model and are not to be construed as limiting the scope of the utility model. The utility model is more particularly described by way of example in the following paragraphs with reference to the drawings. The advantages and features of the present utility model will become more apparent from the following description. It should be noted that the drawings are in a very simplified form and are all to a non-precise scale, merely for convenience and clarity in aiding in the description of embodiments of the utility model.
It will be understood that when an element is referred to as being "fixed to" another element, it can be directly on the other element or intervening elements may also be present. When a component is considered to be "connected" to another component, it can be directly connected to the other component or intervening components may also be present. When an element is referred to as being "disposed on" another element, it can be directly on the other element or intervening elements may also be present. The terms "vertical," "horizontal," "left," "right," and the like are used herein for illustrative purposes only.
Unless defined otherwise, all technical and scientific terms used herein have the same meaning as commonly understood by one of ordinary skill in the art to which this utility model belongs. The terminology used herein in the description of the utility model is for the purpose of describing particular embodiments only and is not intended to be limiting of the utility model. The term "and/or" as used herein includes any and all combinations of one or more of the associated listed items.
The utility model is further illustrated by the following examples in conjunction with the accompanying drawings:
the utility model relates to an ozone flow distributor for advanced oxidation reaction of sewage treatment, which is a set of integrated device for distributing ozone flow in advanced oxidation treatment process, and the system comprises an integral skid-mounted frame 1, a pipeline support frame 2, a main air inlet pipeline 3, a main air inlet 4, a blind plate 5, a pipeline fixing clamp 6, a branch gas pipeline 7, a gas regulating valve 8, a rotameter 9, a meter valve 10, a pressure gauge 11 and an air outlet 12.
The concrete structure is as shown in fig. 1 to 3, whole sled dress frame 1 includes chassis 101 and erects frame 102, chassis 101, erects frame 102 and becomes the shape of falling T and arrange, install main air intake duct 3 through a plurality of pipeline support frame 2 on chassis 101 at erects frame 102 front side, main air intake duct 3 one end is equipped with main air inlet 4 and installs blind plate 5 in other one end, main air inlet 4 is equipped with the inlet connection flange dish, install the branch gas pipeline 7 of a plurality of vertical distribution through pipeline fixing clip 6 in erects frame 102 front side, all be equipped with gas regulating valve 8 on every branch gas pipeline 7 from the bottom up in proper order, rotor flowmeter 9 and table valve 10, install manometer 11 on the table valve 10, every branch gas pipeline 7 top all bends and is equipped with gas outlet 12, gas outlet 12 is equipped with the connection flange dish of giving vent to anger.
The main air inlet pipeline 3 can realize that any one of two ends can be subjected to air inlet, so that the on-site connection is facilitated, one end is connected by using a flange, and the other end is blocked by using a blind plate 5; the upper part of the main air inlet pipeline 3 is welded with a branch air pipeline 7, so that the air is conveniently split.
The branch gas pipeline 7 is fixed on the integral skid-mounted frame 1 through a pipeline fixing clamp 6.
The gas regulating valve 8 is connected to the upper side of the branch gas pipeline 7 through a flange, so that the gas regulating valve is convenient for regulating the gas quantity of each branch.
The rotameter 9 is arranged above the gas regulating valve 8 of the branch gas pipeline 7, and the front and back of the rotameter 9 are required to meet the front ten-time pipe diameter and the back five-time pipe diameter, so that the flow is ensured to be displayed correctly.
The pressure gauge 11 and the gauge valve 10 are fixed above the rotameter 9, so that the end pipeline can be prevented from being blocked or gas leakage; the meter valve 10 can ensure the normal operation of the system when the pressure meter 11 fails through a switch.
The air outlets 12 of the branch air pipelines 7 are positioned at the uppermost part and are connected with the reaction zones of each stage in a path through flange connection.
Reinforcing diagonal braces 103 are arranged between the left side and the right side of the upper surface of the underframe 101 and the vertical frame 102, the reinforcing diagonal braces 103 and the main air inlet pipeline 3 are distributed on the two sides of the vertical frame 102, a plurality of L-shaped mounting plates 104 are welded on the bottom of the underframe 101, and mounting holes 105 are formed in horizontal plates of the L-shaped mounting plates 104.
The pipeline support frame 2 comprises a support frame 201 arranged below the main air inlet pipeline 3, support columns 202 are fixedly arranged between four corners of the bottom of the support frame 201 and the upper surface of the underframe 101, n-shaped pipe clamps 203 are arranged on the left side and the right side of the upper surface of the support frame 201, the n-shaped pipe clamps 203 are wound on the main air inlet pipeline 3, fixed lug plates 204 are arranged on the front side and the rear side of the bottom of the n-shaped pipe clamps 203, and the fixed lug plates 204 are arranged on the support frame 201 through bolts.
The pipeline fixing clamp 6 comprises two semicircular pipe clamps 601 clamped on the front side and the rear side of the branched gas pipeline 7, connecting lug plates 602 are arranged on the left side and the right side of the semicircular pipe clamps 601, the connecting lug plates 602 corresponding to the two semicircular pipe clamps 601 are connected through bolts, and a connecting rod 603 is fixedly arranged between the middle position of the outer wall of the semicircular pipe clamp 601 close to the vertical frame 102 and the vertical frame 102.
The utility model adjusts the gas quantity required by each process section through the gas regulating valve 8, and realizes the gas quantity of each process section through the display of the rotameter 9.
The utility model realizes the display of the air supply pressure of each process section through the pressure gauge 11, and prevents the pipeline from being blocked or gas leakage.
The utility model adopts the anti-corrosion material to prevent the ozone gas from corroding.
According to the utility model, deoiling and degreasing treatment is required for all pipelines, so that the pipelines are ensured to be clean before use.
The utility model realizes the matching of the main air inlet pipeline 3 and each branch air pipeline 7 through CFD simulation.
The utility model can effectively realize the uniform and accurate ozone addition in each stage of reaction area, ensure the uniform aeration at the tail end and realize the efficient mixing of ozone in water.
The utility model is a skid-mounted structure integrating all parts, and can be placed above a reaction zone, thereby being convenient for unified operation and adjustment. The whole sled dress frame 1 is above each part integrated carrier, guarantees that each part is fixed stable, and whole sled dress simultaneously realizes that ozone flow distributor can place in reaction zone upper portion, is convenient for unify operation and regulation.
The integrated skid-mounted distributor is used as a set of integrated skid-mounted distributor, gas is introduced through the main gas inlet pipeline 3, the flow is regulated through the gas regulating valve 8 of each stage of branch gas pipeline 7, the flow display of each stage is realized through observing the rotameter 9, meanwhile, the blocking of the tail end pipeline or the leakage of the gas can be prevented through the display of the pressure gauge 11, the ozone pipelines of each reaction area are connected to the gas outlet 12 through the flange, the gas enters each reaction area, the ozone addition of each reaction area is participated, the uniform and accurate ozone addition is ensured, the uniform aeration of the tail end is ensured, and the efficient mixing of the ozone in water is realized.
While the utility model has been described above with reference to the accompanying drawings, it will be apparent that the utility model is not limited to the above embodiments, but is intended to cover various modifications, either made by the method concepts and technical solutions of the utility model, or applied directly to other applications without modification, within the scope of the utility model.
Claims (7)
1. The utility model provides an ozone flow distributor for sewage treatment advanced oxidation, a serial communication port, including whole sled dress frame (1), whole sled dress frame (1) is including chassis (101) and erects frame (102), chassis (101), erect frame (102) and become the shape of falling T and arrange, install main air intake duct (3) at erectting frame (102) front side through a plurality of pipeline support frame (2) on chassis (101), main air intake duct (3) one end is equipped with main air inlet (4) and blind plate (5) are installed to other one end, it installs branch gas pipeline (7) of a plurality of vertical distribution through pipeline fixing clip (6) to erect frame (102) front side, all be equipped with gas regulating valve (8) on every branch gas pipeline (7) from the bottom up in proper order, rotor flowmeter (9) and table valve (10), install manometer (11) on table valve (10), every branch gas pipeline (7) top all bends and is equipped with gas outlet (12).
2. The ozone flow distributor for advanced oxidation reaction of sewage treatment according to claim 1, wherein a reinforcing diagonal brace (103) is arranged between the left side and the right side of the upper surface of the underframe (101) and the vertical frame (102), and the reinforcing diagonal brace (103) and the main air inlet pipeline (3) are distributed on two sides of the vertical frame (102).
3. The ozone flow distributor for advanced oxidation reaction of sewage treatment according to claim 2, wherein the pipeline supporting frame (2) comprises a supporting frame (201) arranged below the main air inlet pipeline (3), supporting columns (202) are fixedly arranged between four corners of the bottom of the supporting frame (201) and the upper surface of the underframe (101), n-shaped pipe clamps (203) are arranged on the left side and the right side of the upper surface of the supporting frame (201), the n-shaped pipe clamps (203) are wound on the main air inlet pipeline (3), fixed lug plates (204) are arranged on the front side and the rear side of the bottom of the n-shaped pipe clamps (203), and the fixed lug plates (204) are arranged on the supporting frame (201) through bolts.
4. The ozone flow distributor for advanced oxidation reaction of sewage treatment according to claim 3, wherein the pipeline fixing clamp (6) comprises two semicircular pipe clamps (601) clamped on the front side and the rear side of the branched gas pipeline (7), connecting lug plates (602) are arranged on the left side and the right side of each semicircular pipe clamp (601), the corresponding connecting lug plates (602) of the two semicircular pipe clamps (601) are connected through bolts, and a connecting rod (603) is fixedly arranged between the middle position of the outer wall of each semicircular pipe clamp (601) close to the vertical frame (102) and the vertical frame (102).
5. The ozone flow distributor for advanced oxidation reaction in sewage treatment according to claim 4, wherein a plurality of L-shaped mounting plates (104) are welded at the bottom of the underframe (101), and mounting holes (105) are formed in the horizontal plates of the L-shaped mounting plates (104).
6. An ozone flow distributor for advanced oxidation reactions in sewage treatment according to claim 5 wherein the primary air inlet (4) is provided with an inlet connection flange.
7. An ozone flow distributor for advanced oxidation reactions in sewage treatment according to claim 6 wherein the air outlet (12) is provided with an air outlet connection flange.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202321931939.0U CN220502793U (en) | 2023-07-21 | 2023-07-21 | Ozone flow distributor for advanced oxidation reaction of sewage treatment |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202321931939.0U CN220502793U (en) | 2023-07-21 | 2023-07-21 | Ozone flow distributor for advanced oxidation reaction of sewage treatment |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN220502793U true CN220502793U (en) | 2024-02-20 |
Family
ID=89871881
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN202321931939.0U Active CN220502793U (en) | 2023-07-21 | 2023-07-21 | Ozone flow distributor for advanced oxidation reaction of sewage treatment |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN220502793U (en) |
-
2023
- 2023-07-21 CN CN202321931939.0U patent/CN220502793U/en active Active
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