CN219689472U - Pipeline type Gao Xiaofen ton reaction device - Google Patents
Pipeline type Gao Xiaofen ton reaction device Download PDFInfo
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- CN219689472U CN219689472U CN202320873894.XU CN202320873894U CN219689472U CN 219689472 U CN219689472 U CN 219689472U CN 202320873894 U CN202320873894 U CN 202320873894U CN 219689472 U CN219689472 U CN 219689472U
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- baffling
- reaction device
- xiaofen
- dispersion
- baffle
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- 238000006243 chemical reaction Methods 0.000 title claims abstract description 42
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 68
- 239000006185 dispersion Substances 0.000 claims abstract description 34
- 238000009434 installation Methods 0.000 claims description 6
- 238000005273 aeration Methods 0.000 abstract description 9
- 230000000694 effects Effects 0.000 abstract description 8
- 239000006260 foam Substances 0.000 abstract description 6
- 230000035484 reaction time Effects 0.000 abstract description 6
- 238000003756 stirring Methods 0.000 abstract description 5
- 238000004519 manufacturing process Methods 0.000 abstract description 2
- 230000005465 channeling Effects 0.000 abstract 1
- 230000002708 enhancing effect Effects 0.000 abstract 1
- 239000002351 wastewater Substances 0.000 description 6
- 238000010586 diagram Methods 0.000 description 3
- 230000005587 bubbling Effects 0.000 description 2
- 239000000203 mixture Substances 0.000 description 2
- 238000010992 reflux Methods 0.000 description 2
- 238000005728 strengthening Methods 0.000 description 2
- 230000009286 beneficial effect Effects 0.000 description 1
- 238000012993 chemical processing Methods 0.000 description 1
- 238000010276 construction Methods 0.000 description 1
- 230000007547 defect Effects 0.000 description 1
- 239000012530 fluid Substances 0.000 description 1
- 239000007791 liquid phase Substances 0.000 description 1
- 238000000034 method Methods 0.000 description 1
- 239000002994 raw material Substances 0.000 description 1
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- Treatment Of Water By Oxidation Or Reduction (AREA)
Abstract
The utility model discloses a pipeline type Gao Xiaofen ton reaction device which comprises two baffle box body supports, wherein a baffle water inlet box is arranged at the bottom of one baffle box body support, a baffle water outlet tank is arranged at the top of the other baffle box body support, a mixed flow pipe support is arranged between the two baffle box body supports, and a pipeline reactor is arranged on the mixed flow pipe support. The utility model can greatly shorten the reaction time by adopting the design of the pipeline reactor and enhancing the reaction effect by arranging the cyclone dispersion plate in the pipeline reactor, reduce the foam production, facilitate the subsequent treatment, avoid the problems that the existing Fenton reaction device needs longer residence reaction time and larger occupied area of the reaction device, the reaction effect of pneumatic stirring due to overlarge aeration bubbles is poor, and the reactor is easy to produce a large amount of foam and generate the phenomenon of channeling due to overlarge aeration bubbles.
Description
Technical Field
The utility model relates to the technical field of chemical processing, in particular to a pipeline type Gao Xiaofen ton reaction device.
Background
The existing Fenton reaction device is usually a tower reactor, the required residence reaction time is longer, the occupied area of the reaction device is larger, the reaction effect of pneumatic stirring is poor due to overlarge aeration bubbles in the reactor usually in an aeration strengthening reaction process, a large amount of foam is easily generated in the reactor due to overlarge aeration bubbles, the phenomenon of bubbling is generated, and the working efficiency is lower.
Disclosure of Invention
The utility model aims to overcome the defects that the existing Fenton reaction device needs longer residence reaction time, the reaction device occupies larger area, the reaction effect of pneumatic stirring is poor due to overlarge aeration bubbles in the reaction process, and the reaction device is easy to generate a large amount of foam and generate a groove overflowing phenomenon due to overlarge aeration bubbles, and the pipeline type Gao Xiaofen ton reaction device is provided.
In order to achieve the above purpose, the present utility model adopts the following technical scheme:
the utility model provides a pipeline formula Gao Xiaofen ton reaction unit, includes two baffling railway carriage or compartment body supports, and the bottom of one of them baffling railway carriage or compartment body support is equipped with the baffling water inlet box, and the top of another baffling railway carriage or compartment body support is equipped with the roll-over water tank, is equipped with the mixed flow pipe support between two baffling railway carriage or compartment body supports, the mixed flow pipe support on install the pipeline reactor, the pipeline reactor in set up the dispersion and mix the flow ware, the dispersion mix and be equipped with a plurality of whirl dispersion dish on the flow ware, be provided with a plurality of dispersion poles on every whirl dispersion dish, whirl dispersion dish one side be equipped with the water conservancy diversion dish, the water conservancy diversion dish on be equipped with a plurality of water conservancy diversion holes, water conservancy diversion dish and dispersion pole all be located one side of intaking.
Preferably, the mixed flow pipe support is provided with a circulating pump, the circulating pump is connected with an internal circulating water inlet, and the internal circulating water inlet is connected with a baffling water inlet box.
Preferably, the baffling water inlet box is connected with a main water inlet, and the baffling water outlet box is connected with a main water outlet.
Preferably, the circulating pump is connected with an internal circulating water outlet, and the internal circulating water outlet is connected with a baffling water outlet tank.
Preferably, a baffle connection box is arranged at the top of one of the baffle box body brackets, and the baffle connection box is positioned at the upper part of the baffle water inlet box.
Preferably, the dispersing mixer is internally provided with a fixed rod, the guide disc is arranged on the fixed rod, the fixed rod is provided with an installation cylinder, the cyclone dispersing disc is arranged on the installation cylinder, and the dispersing rod is annularly arranged on the surface of the cyclone dispersing disc.
Compared with the prior art, the utility model has the beneficial effects that:
1. the whole reaction device adopts a bedroom cross flow circulation mode, does not store gas to generate supercharging, and the flow velocity of fluid in a pipeline reactor is 1-3m/s
A baffle plate is arranged in the pipeline connecting box, and the inclination angle of the baffle plate is 30-50 degrees;
2. a dispersing mixer is arranged in the pipeline reactor, the dispersing mixer consists of a flow equalizing disc and a dispersing disc, the design of a baffling water outlet box adopts a water outlet mode, gas generated in the reaction process is discharged upwards, and backflow gas is prevented from entering a circulating pump to cause cavitation of a pump impeller, and the backflow ratio of wastewater is 100-500%;
in summary, the utility model can greatly shorten the reaction time by adopting the design of the pipeline reactor and strengthening the reaction effect by arranging the cyclone dispersion plate in the pipeline reactor, reduce the size specification of the reactor and the occupied area, strengthen the turbulence degree of the liquid phase in the pipeline by adopting a mode of large reflux ratio of an internal circulating pump, and compared with the pneumatic stirring effect, the utility model has better foam production, is more convenient for subsequent treatment, avoids the problems that the existing Fenton reaction device needs longer stay reaction time, the occupied area of the reaction device is larger, the reaction effect of pneumatic stirring is poor due to overlarge aeration bubbles in the reaction process, and the reactor is easy to produce a large amount of foam due to overlarge aeration bubbles, thereby generating the phenomenon of bubbling.
Drawings
FIG. 1 is a block diagram of a pipe-type Gao Xiaofen ton reaction device according to the present utility model;
FIG. 2 is a schematic diagram of the internal structure of a pipe-type Gao Xiaofen ton reaction device according to the present utility model;
FIG. 3 is a side view of a piping type Gao Xiaofen ton reaction device according to the present utility model;
FIG. 4 is a side view of a side internal construction of a pipe-type Gao Xiaofen ton reaction device according to the present utility model;
FIG. 5 is a block diagram of a flow mixer of a pipe type Gao Xiaofen ton reaction device according to the present utility model;
fig. 6 is a side view of a dispersion mixer of a pipe type Gao Xiaofen ton reaction device according to the present utility model.
In the figure: 1. an internal circulation water inlet; 2. a main water inlet; 3. baffling the water inlet box; 4. a baffling connection box; 5. a mixed flow pipe bracket; 6. a dispersion mixer; 7. a main water outlet; 8. the water flows out of the water tank; 9. an internal circulation water outlet; 10. a pipeline reactor; 11. a circulation pump; 12. a baffle box body bracket; 13. a swirl dispersion plate; 14. a fixed rod; 15. a deflector disc; 16. a deflector aperture; 17. a mounting cylinder; 18. a dispersion bar.
Detailed Description
In order that the above-recited objects, features and advantages of the present utility model will become more apparent, a more particular description of the utility model will be rendered by reference to specific embodiments thereof which are illustrated in the appended drawings.
In the following description, numerous specific details are set forth in order to provide a thorough understanding of the present utility model, but the present utility model may be practiced in other ways other than those described herein, and persons skilled in the art will readily appreciate that the present utility model is not limited to the specific embodiments disclosed below.
Further, reference herein to "one embodiment" or "an embodiment" means that a particular feature, structure, or characteristic can be included in at least one implementation of the utility model. The appearances of the phrase "in one embodiment" in various places in the specification are not necessarily all referring to the same embodiment, nor are separate or alternative embodiments mutually exclusive of other embodiments.
The raw materials used in the examples were commercially purchased unless otherwise specified.
Referring to FIGS. 1-6, a pipeline type Gao Xiaofen ton reaction device comprises two baffle box body brackets 12, wherein a baffle water inlet box 3 is arranged at the bottom of one baffle box body bracket 12, a baffle connecting box 4 is arranged at the top, the baffle connecting box 4 is positioned at the upper part of the baffle water inlet box 3, a main water inlet 2 is connected to the baffle water inlet box 3 and used for entering waste water, a main water outlet 7 is connected to a baffle water tank 8 and used for delivering water flow after Fenton reaction, a baffle water tank 8 is arranged at the top of the other baffle box body bracket 12, a mixed flow pipe bracket 5 is arranged between the two baffle box body brackets 12, a pipeline reactor 10 is arranged on the mixed flow pipe bracket 5, a dispersing mixed flow device 6 is arranged in the pipeline reactor 10, a plurality of cyclone dispersing discs 13 are arranged on the dispersing mixed flow device 6, each cyclone dispersion plate 13 is provided with a plurality of dispersion rods 18, one side of each cyclone dispersion plate 13 is provided with a guide plate 15, the guide plate 15 is provided with a plurality of guide holes 16, the guide plate 15 and the dispersion rods 18 are all positioned on one side of water inflow, water flow is dispersed, a fixed rod 14 is arranged in the dispersion mixer 6, the guide plate 15 is arranged on the fixed rod 14, the fixed rod 14 is provided with an installation cylinder 17, the cyclone dispersion plate 13 is arranged on the installation cylinder 17, the dispersion rods 18 are annularly arranged on the surface of the cyclone dispersion plate 13, the guide plate 15 and the cyclone dispersion plate 13 are all fixed on the fixed rod 14, water flow is driven by a circulating pump 11 and is sent into a pipeline reactor 10, and is sent into the cyclone dispersion plate 13 through the guide holes 16 on the guide plate 15, and is dispersed through the dispersion rods 18 annularly arranged on the cyclone dispersion plate 13, so that the reaction effect is enhanced.
In the utility model, a circulating pump 11 is arranged on a mixed flow pipe bracket 5, an internal circulating water inlet 1 is connected to the circulating pump 11, the internal circulating water inlet 1 is connected with a baffling water inlet box 3, an internal circulating water outlet 9 is connected to the circulating pump 11, and the internal circulating water outlet 9 is connected with a baffling water outlet box 8 for conveying water flow.
In the utility model, wastewater enters the baffling water inlet box 3 through a water inlet and is mixed with internal circulation water, then continuously passes through the pipeline reactor 10 and the baffling connecting box 4 which are provided with the dispersion mixer 6, finally enters the baffling water outlet box, the wastewater after full reaction is discharged through the main water outlet 7, and a certain proportion of wastewater is returned through a reflux pump and is mixed with new wastewater to repeat the process.
It should be noted that the above embodiments are only for illustrating the technical solution of the present utility model and not for limiting the same, and although the present utility model has been described in detail with reference to the preferred embodiments, it should be understood by those skilled in the art that the technical solution of the present utility model may be modified or substituted without departing from the spirit and scope of the technical solution of the present utility model, which is intended to be covered in the scope of the claims of the present utility model.
Claims (6)
1. The utility model provides a pipeline formula Gao Xiaofen ton reaction unit, includes two baffling railway carriage or compartment body supports (12), characterized by, the bottom of one of them baffling railway carriage or compartment body support (12) is equipped with baffling water inlet box (3), and the top of another baffling railway carriage or compartment body support (12) is equipped with rolls over outflow water tank (8), is equipped with mixed flow pipe support (5) between two baffling railway carriage or compartment body supports (12), mixed flow pipe support (5) on install pipeline reactor (10), pipeline reactor (10) in set up scattered mixed flow ware (6), scattered mixed flow ware (6) on be equipped with a plurality of whirl dispersion dish (13), be provided with a plurality of dispersion poles (18) on every whirl dispersion dish (13), whirl dispersion dish (13) one side be equipped with water conservancy diversion dish (15), water conservancy diversion dish (15) on be equipped with a plurality of water conservancy diversion holes (16), water conservancy diversion dish (15) and dispersion pole (18) all be located one side of intaking.
2. The pipeline type Gao Xiaofen ton reaction device according to claim 1, wherein a fixed rod (14) is arranged in the dispersing mixer (6), the guide disc (15) is installed on the fixed rod (14), an installation cylinder (17) is arranged on the fixed rod (14), the cyclone dispersion disc (13) is installed on the installation cylinder (17), and the dispersion rod (18) is installed on the surface of the cyclone dispersion disc (13) in a ring shape.
3. The pipeline type Gao Xiaofen ton reaction device according to claim 1, wherein the mixed flow pipe support (5) is provided with a circulating pump (11), the circulating pump (11) is connected with an internal circulating water inlet (1), and the internal circulating water inlet (1) is connected with a baffling water inlet box (3).
4. A pipeline type Gao Xiaofen ton reaction device according to claim 3, wherein the baffling water inlet box (3) is connected with a main water inlet (2), and the baffling water outlet box (8) is connected with a main water outlet (7).
5. The pipeline type Gao Xiaofen ton reaction device according to claim 4, wherein the circulating pump (11) is connected with an internal circulating water outlet (9), and the internal circulating water outlet (9) is connected with a baffling water outlet tank (8).
6. A pipeline type Gao Xiaofen ton reaction device according to claim 1, wherein a baffle connection box (4) is arranged at the top of one baffle box body bracket (12), and the baffle connection box (4) is positioned at the upper part of the baffle water inlet box (3).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202320873894.XU CN219689472U (en) | 2023-04-19 | 2023-04-19 | Pipeline type Gao Xiaofen ton reaction device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202320873894.XU CN219689472U (en) | 2023-04-19 | 2023-04-19 | Pipeline type Gao Xiaofen ton reaction device |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN219689472U true CN219689472U (en) | 2023-09-15 |
Family
ID=87966548
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN202320873894.XU Active CN219689472U (en) | 2023-04-19 | 2023-04-19 | Pipeline type Gao Xiaofen ton reaction device |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN219689472U (en) |
-
2023
- 2023-04-19 CN CN202320873894.XU patent/CN219689472U/en active Active
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