CN220012309U - Novel ozone reaction tower structure - Google Patents
Novel ozone reaction tower structure Download PDFInfo
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- CN220012309U CN220012309U CN202320867062.7U CN202320867062U CN220012309U CN 220012309 U CN220012309 U CN 220012309U CN 202320867062 U CN202320867062 U CN 202320867062U CN 220012309 U CN220012309 U CN 220012309U
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- water
- reaction tower
- catalytic layer
- ozone
- air duct
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- 238000006243 chemical reaction Methods 0.000 title claims abstract description 64
- CBENFWSGALASAD-UHFFFAOYSA-N Ozone Chemical compound [O-][O+]=O CBENFWSGALASAD-UHFFFAOYSA-N 0.000 title claims abstract description 58
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 105
- 230000003197 catalytic effect Effects 0.000 claims abstract description 57
- 230000000149 penetrating effect Effects 0.000 claims abstract description 5
- 239000007788 liquid Substances 0.000 claims description 14
- 238000001914 filtration Methods 0.000 claims description 5
- 239000007789 gas Substances 0.000 description 28
- 239000002351 wastewater Substances 0.000 description 26
- 239000003054 catalyst Substances 0.000 description 6
- 238000005457 optimization Methods 0.000 description 6
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 3
- 238000000034 method Methods 0.000 description 3
- 230000003647 oxidation Effects 0.000 description 3
- 238000007254 oxidation reaction Methods 0.000 description 3
- 239000001301 oxygen Substances 0.000 description 3
- 229910052760 oxygen Inorganic materials 0.000 description 3
- 238000012216 screening Methods 0.000 description 3
- 238000004065 wastewater treatment Methods 0.000 description 3
- 238000010586 diagram Methods 0.000 description 2
- 239000012535 impurity Substances 0.000 description 2
- 230000033116 oxidation-reduction process Effects 0.000 description 2
- 238000000926 separation method Methods 0.000 description 2
- 238000005507 spraying Methods 0.000 description 2
- 230000001954 sterilising effect Effects 0.000 description 2
- 230000009286 beneficial effect Effects 0.000 description 1
- 230000015556 catabolic process Effects 0.000 description 1
- 238000010276 construction Methods 0.000 description 1
- 238000004042 decolorization Methods 0.000 description 1
- 238000006731 degradation reaction Methods 0.000 description 1
- 238000004332 deodorization Methods 0.000 description 1
- 230000001877 deodorizing effect Effects 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 125000002887 hydroxy group Chemical group [H]O* 0.000 description 1
- 239000010842 industrial wastewater Substances 0.000 description 1
- 231100001240 inorganic pollutant Toxicity 0.000 description 1
- 239000000543 intermediate Substances 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 230000035515 penetration Effects 0.000 description 1
- 238000005086 pumping Methods 0.000 description 1
- 238000004659 sterilization and disinfection Methods 0.000 description 1
Landscapes
- Treatment Of Water By Oxidation Or Reduction (AREA)
Abstract
The utility model discloses a novel ozone reaction tower structure, which comprises a reaction tower, a water storage tank arranged on the upper end surface of the reaction tower, an ozone converter arranged on the right side of the reaction tower and a raw water barrel arranged on the left end of the reaction tower, wherein the reaction tower is communicated with the water storage tank through a water guide pipe and extends into the reaction tower, the lower end of the water guide pipe is fixedly connected with a water sprinkling disc, a plurality of uniformly distributed water dripping holes are formed in the upper end surface of the water sprinkling disc in a penetrating way, water diversion grooves formed in the upper end surface of the water sprinkling disc are communicated between the water dripping holes and the water guide pipe, two first catalytic layers and second catalytic layers which are distributed from top to bottom are arranged in the reaction tower, the other ends of a plurality of second air guide pipes and third air guide pipes extend into the first catalytic layers and the second catalytic layers respectively.
Description
Technical Field
The utility model relates to the technical field of wastewater treatment, in particular to a novel ozone reaction tower structure.
Background
Ozone has very high oxidation-reduction potential (2.07V), generates hydroxyl free radicals (OH, oxidation-reduction potential 2.80V) and other oxidation intermediates with stronger oxidation capability after being decomposed in water, can react with organic and inorganic pollutants in the water to achieve the purposes of deodorizing, decoloring, sterilizing and removing organic matters, and industrial wastewater has the characteristics of high COD, high chromaticity, high turbidity, low biochemistry, difficult degradation of organic matters in the water and the like, so that the novel ozone reaction tower structure is very necessary to be produced by combining the oxidation technology of ozone.
The traditional wastewater treatment mode widely adopts a solid-liquid separation screening device, and the solid-liquid separation screening device generally comprises a screening structure and a liquid collecting structure, and the operation steps generally comprise: firstly pouring the wastewater into the device, separating impurities in the wastewater to the upper end of the screen through the filtration of the screen, filtering the filtered wastewater through other screens with smaller meshes, and collecting the filtered wastewater into a liquid collecting device through a honeycomb duct through repeated filtration layer by layer.
Although the method can realize the purpose of wastewater treatment, the method adopts screens with different mesh sizes to filter the wastewater layer by layer, and can remove some impurities with larger volume, but the organic matters which are difficult to degrade and have smaller volume are difficult to thoroughly clean, and along with the gradual implementation of the comprehensive wastewater discharge standard, the original treatment process is difficult to reach the wastewater discharge standard.
Disclosure of Invention
The utility model aims to provide a novel ozone reaction tower structure which has the advantages of uniform sprinkling, full reaction of ozone gas with wastewater through a catalyst, and convenience for full deodorization, decolorization, sterilization and removal of organic matters and inorganic matters.
In order to achieve the above purpose, the present utility model provides the following technical solutions: the utility model provides a novel ozone reaction tower structure, includes the reaction tower, installs the storage water tank at the reaction tower up end, is located the ozone converter on reaction tower right side and is located the raw water bucket of reaction tower left end, the reaction tower passes through the aqueduct intercommunication with the storage water tank and extends to inside the reaction tower, the lower extreme fixedly connected with watering dish of aqueduct, a plurality of evenly distributed's drip holes have been seted up in the up end penetration of watering dish, a plurality of all be linked together between drip hole and the aqueduct and set up the water guide slot at the up end of watering dish, the lower terminal surface of watering dish is installed and is corresponding drip hole site's drip pipe
The inside of reaction tower installs two from last first catalytic layer and the second catalytic layer that distributes down, the first air duct that extends to the inside of reaction tower is installed to ozone converter's one end, first air duct is located between first catalytic layer and the second catalytic layer, first air duct outer wall intercommunication has a plurality of evenly distributed's second air duct and third air duct, a plurality of the other end of second air duct and third air duct extends to the inside of first catalytic layer and second catalytic layer respectively.
In order to enable ozone gas to enter the first catalytic layer and the second catalytic layer through the second air guide pipe and the third air guide pipe respectively, the novel ozone reaction tower structure is preferable, and a plurality of evenly distributed air outlet pipes are arranged on the outer walls of the second air guide pipe and the third air guide pipe.
In order to enable the wastewater to flow into the first catalytic layer and the second catalytic layer, the novel ozone reaction tower structure is preferable, and a plurality of uniformly distributed filtering holes are formed in the outer walls of the first catalytic layer and the second catalytic layer in a penetrating manner.
In order to facilitate the discharge of unused ozone into oxygen, the novel ozone reaction tower structure is preferable, and the upper end of the right side of the outer wall of the reaction tower is fixedly connected with an ozone destructor through an exhaust pipe.
In order to facilitate the ozone to enter the catalytic layer, control the flow of the gas and monitor the flow of the gas, the novel ozone reaction tower structure is preferable, and a draught fan, a gas valve and a gas flowmeter are sequentially arranged in the first gas guide pipe positioned on the right side of the reaction tower from top to bottom.
In order to facilitate the wastewater to enter a water storage tank from a raw water barrel, control the flow of the wastewater and monitor the flow of the wastewater, the novel ozone reaction tower structure is preferable, the water storage tank is communicated with the raw water barrel through a water suction pipe, and a water suction pump, a liquid valve and a liquid flowmeter are sequentially arranged in the water suction pipe from top to bottom.
In order to facilitate the removal of oxidized water energy, the novel ozone reaction tower structure is preferable, and a water outlet is arranged at the lower end of the left side of the outer wall of the reaction tower.
Compared with the prior art, the utility model has the following beneficial effects:
the novel ozone reaction tower structure adopts the mode that the lower end of the water guide pipe is connected with the water sprinkling disc, the upper end surface of the water sprinkling disc is penetrated and provided with the water dripping hole, and the water guide groove is connected with the water dripping hole and the water guide pipe, so that water flow can be uniformly sprinkled into the first catalytic layer and the second catalytic layer;
the first air duct is connected with the ozone converter, the second air duct and the third air duct which are uniformly distributed are connected to the outer wall of the first air duct, and gas can be uniformly introduced into the first catalytic layer and the second catalytic layer, so that the reaction efficiency of ozone through the catalyst and wastewater is improved.
Drawings
FIG. 1 is a block diagram of the overall cross-section of the present utility model;
FIG. 2 is a diagram of the external structure of the fitting body of the present utility model;
FIG. 3 is a view showing the construction of the whole outer part of the sprinkler;
FIG. 4 is a front view of the sprinkler pan of the present utility model;
in the figure: 1. a reaction tower; 2. a water storage tank; 3. an ozone converter; 4. raw water barrel; 5. a water conduit; 6. a watering plate; 7. a drip hole; 8. a water diversion trench; 9. a drip tube; 10. a first catalytic layer; 11. a second catalytic layer; 12. a first air duct; 13. a second air duct; 14. a third air duct; 15. an air outlet pipe; 16. a filter hole; 17. an exhaust pipe; 18. an ozone destructor; 19. an induced draft fan; 20. a gas valve; 21. a gas flow meter; 22. a water pumping pipe; 23. a water pump; 24. a liquid valve; 25. a liquid flow meter; 26. and a water outlet.
Detailed Description
Referring to fig. 1 to 4, a novel ozone reaction tower structure comprises a reaction tower 1, a water storage tank 2 arranged on the upper end surface of the reaction tower 1, an ozone converter 3 positioned on the right side of the reaction tower 1 and a raw water barrel 4 positioned at the left end of the reaction tower 1, wherein the reaction tower 1 is communicated with the water storage tank 2 through a water guide pipe 5 and extends into the reaction tower 1, the lower end of the water guide pipe 5 is fixedly connected with a water sprinkling disc 6, a plurality of uniformly distributed water dripping holes 7 are formed in the upper end surface of the water sprinkling disc 6 in a penetrating manner, water guiding grooves 8 formed in the upper end surface of the water sprinkling disc 6 are communicated between the plurality of water dripping holes 7 and the water guide pipe 5, and a water dripping pipe 9 corresponding to the water dripping holes is arranged on the lower end surface of the water sprinkling disc 6;
the inside of the reaction tower 1 is provided with a first catalytic layer 10 and a second catalytic layer 11 which are distributed from top to bottom, one end of the ozone converter 3 is provided with a first air duct 12 which extends into the reaction tower 1, the first air duct 12 is positioned between the first catalytic layer 10 and the second catalytic layer 11, the outer wall of the first air duct 12 is communicated with a plurality of second air ducts 13 and third air ducts 14 which are uniformly distributed, and the other ends of the second air ducts 13 and the third air ducts 14 respectively extend into the first catalytic layer 10 and the second catalytic layer 11.
In this embodiment: before the waste water is oxidized, the waste water in the water storage tank 2 flows into a water diversion groove 8 formed in the upper end face of the water spraying disc 6 along the water diversion pipe 5, the waste water flows into a water dripping hole 7 along the water diversion groove 8, then flows into a water dripping pipe 9 along the water dripping hole 7, and is sprayed to the first catalytic layer 10, so that the effect that the waste water in the water storage tank 2 can be uniformly dispersed on the upper end face of the first catalytic layer 10 is achieved;
the ozone converter 3 converts oxygen into ozone gas, the first air duct 12 introduces the ozone gas into the plurality of second air ducts 13 and the plurality of third air ducts 14, and then the ozone gas is dispersed inside the first catalytic layer 10 and the second catalytic layer 11, so that the ozone gas can be uniformly distributed to the first catalytic layer 10 and the second catalytic layer 11.
As a technical optimization scheme of the utility model, a plurality of evenly distributed air outlet pipes 15 are arranged on the outer walls of the second air guide pipe 13 and the third air guide pipe 14.
In this embodiment: when ozone gas enters the second gas guide pipe 13 and the third gas guide pipe 14, the gas outlet pipe 15 can facilitate the ozone gas to enter the first catalytic layer 10 and the second catalytic layer 11 respectively.
As a technical optimization scheme of the present utility model, a plurality of uniformly distributed filter holes 16 are formed through the outer walls of the first catalytic layer 10 and the second catalytic layer 11.
In this embodiment: the filter holes 16 allow the waste water to enter the first catalytic layer 10 and the second catalytic layer 11 when the waste water falls down from the plurality of drip pipes 9.
As a technical optimization scheme of the utility model, the upper end of the right side of the outer wall of the reaction tower 1 is fixedly connected with an ozone destructor 18 through an exhaust pipe 17.
In this embodiment: by providing the ozone destructor 18, the unused ozone can be reconverted into oxygen and discharged from the inside of the reaction tower 1.
As a technical optimization scheme of the utility model, an induced draft fan 19, a gas valve 20 and a gas flowmeter 21 are sequentially arranged in the first gas guide pipe 12 from top to bottom.
In this embodiment: the ozone gas in the first air duct 12 can enter the second air duct 13 and the third air duct 14 along with the induced draft fan 19, and the gas flowmeter 21 can monitor the flow of the ozone gas, so that the gas valve 20 controls the flow of the ozone gas.
As a technical optimization scheme of the utility model, a water storage tank 2 is communicated with a raw water barrel 4 through a water suction pipe 22, and a water suction pump 23, a liquid valve 24 and a liquid flowmeter 25 are sequentially arranged in the water suction pipe 22 from top to bottom.
In this embodiment: by arranging the water suction pump 23, the waste water in the raw water barrel 4 can be pumped into the water storage tank 2, the liquid flowmeter 25 can monitor the waste water flow, and the liquid valve 24 can control the waste water flow.
As a technical optimization scheme of the utility model, a water outlet 26 is arranged at the lower end of the left side of the outer wall of the reaction tower 1.
In this embodiment: the wastewater is purified by the first catalytic layer 10 and the second catalytic layer 11, and the water is discharged from the water outlet 26.
Working principle: before using, the catalyst is filled into the first catalytic layer 10 and the second catalytic layer 11, then the ozone converter 3 is opened to work, ozone gas enters a plurality of second air guide pipes 13 and a plurality of third air guide pipes 14 along with the induced draft fan 19, then enters the first catalytic layer 10 and the second catalytic layer 11 along with the plurality of air outlet pipes 15 to contact with the catalyst, meanwhile, the water suction pump 23 pumps the waste water in the raw water barrel 4 into the water storage tank 2, the waste water in the water storage tank 2 flows into the water guide groove 8 formed on the upper end face of the water spraying disc 6 along the water guide pipe 5, the waste water flows into the drip hole 7 along the water guide groove 8, then enters the drip pipe 9 along the water drip hole 7, and then enters the first catalytic layer 10 to react with ozone and the catalyst, then flows into the second catalytic layer 11, reacts with the ozone and the catalyst, and is discharged from the water outlet 26.
The foregoing description of the preferred embodiments of the utility model is not intended to be limiting, but rather is intended to cover all modifications, equivalents, and alternatives falling within the spirit and principles of the utility model.
Claims (7)
1. The utility model provides a novel ozone reaction tower structure, includes reaction tower (1), installs storage water tank (2) at reaction tower (1) up end, is located ozone converter (3) on reaction tower (1) right side and is located former cask (4) of reaction tower (1) left end, its characterized in that: the reaction tower (1) is communicated with the water storage tank (2) through a water guide pipe (5) and extends into the reaction tower (1), a water sprinkling disc (6) is fixedly connected to the lower end of the water guide pipe (5), a plurality of uniformly distributed water dripping holes (7) are formed in the upper end face of the water sprinkling disc (6) in a penetrating mode, water guide grooves (8) formed in the upper end face of the water sprinkling disc (6) are formed in the positions, corresponding to the positions of the water dripping holes (7), of the lower end face of the water sprinkling disc (6) in a communicating mode;
the inside of reaction tower (1) is installed two from last first catalytic layer (10) and second catalytic layer (11) that distribute down, first air duct (12) that extend to inside reaction tower (1) are installed to the one end of ozone converter (3), first air duct (12) are located between first catalytic layer (10) and second catalytic layer (11), first air duct (12) outer wall intercommunication has a plurality of evenly distributed's second air duct (13) and third air duct (14), a plurality of second air duct (13) and the other end of third air duct (14) extend to the inside of first catalytic layer (10) and with second catalytic layer (11) respectively.
2. The novel ozone reaction tower structure according to claim 1, wherein: a plurality of evenly distributed air outlet pipes (15) are arranged on the outer walls of the second air guide pipe (13) and the third air guide pipe (14).
3. The novel ozone reaction tower structure according to claim 1, wherein: the outer walls of the first catalytic layer (10) and the second catalytic layer (11) are respectively provided with a plurality of uniformly distributed filtering holes (16) in a penetrating way.
4. The novel ozone reaction tower structure according to claim 1, wherein: the upper end of the right side of the outer wall of the reaction tower (1) is fixedly connected with an ozone destructor (18) through an exhaust pipe (17).
5. The novel ozone reaction tower structure according to claim 1, wherein: an induced draft fan (19), a gas valve (20) and a gas flowmeter (21) are sequentially arranged in the first gas guide pipe (12) from top to bottom.
6. The novel ozone reaction tower structure according to claim 1, wherein: the water storage tank (2) is communicated with the raw water barrel (4) through a water suction pipe (22), and a water suction pump (23), a liquid valve (24) and a liquid flowmeter (25) are sequentially arranged in the water suction pipe (22) from top to bottom.
7. The novel ozone reaction tower structure according to claim 1, wherein: a water outlet (26) is arranged at the lower end of the left side of the outer wall of the reaction tower (1).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202320867062.7U CN220012309U (en) | 2023-04-18 | 2023-04-18 | Novel ozone reaction tower structure |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202320867062.7U CN220012309U (en) | 2023-04-18 | 2023-04-18 | Novel ozone reaction tower structure |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN220012309U true CN220012309U (en) | 2023-11-14 |
Family
ID=88684638
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN202320867062.7U Active CN220012309U (en) | 2023-04-18 | 2023-04-18 | Novel ozone reaction tower structure |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN220012309U (en) |
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2023
- 2023-04-18 CN CN202320867062.7U patent/CN220012309U/en active Active
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