CN220537586U - Novel container type ozone advanced oxidation water treatment equipment - Google Patents
Novel container type ozone advanced oxidation water treatment equipment Download PDFInfo
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- CN220537586U CN220537586U CN202322112842.3U CN202322112842U CN220537586U CN 220537586 U CN220537586 U CN 220537586U CN 202322112842 U CN202322112842 U CN 202322112842U CN 220537586 U CN220537586 U CN 220537586U
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- Prior art keywords
- ozone
- water treatment
- advanced oxidation
- oxidation water
- ultraviolet
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- CBENFWSGALASAD-UHFFFAOYSA-N Ozone Chemical compound [O-][O+]=O CBENFWSGALASAD-UHFFFAOYSA-N 0.000 title claims abstract description 98
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 title claims abstract description 51
- 230000003647 oxidation Effects 0.000 title claims abstract description 30
- 238000007254 oxidation reaction Methods 0.000 title claims abstract description 30
- 239000007789 gas Substances 0.000 claims abstract description 42
- 238000002360 preparation method Methods 0.000 claims abstract description 24
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 claims abstract description 22
- 239000001301 oxygen Substances 0.000 claims abstract description 22
- 229910052760 oxygen Inorganic materials 0.000 claims abstract description 22
- 238000006243 chemical reaction Methods 0.000 claims abstract description 21
- 230000006378 damage Effects 0.000 claims abstract description 15
- 239000010865 sewage Substances 0.000 claims abstract description 4
- 238000004140 cleaning Methods 0.000 claims description 43
- 239000007788 liquid Substances 0.000 claims description 31
- MHAJPDPJQMAIIY-UHFFFAOYSA-N Hydrogen peroxide Chemical compound OO MHAJPDPJQMAIIY-UHFFFAOYSA-N 0.000 claims description 12
- 238000000926 separation method Methods 0.000 claims description 10
- 229910001220 stainless steel Inorganic materials 0.000 claims description 7
- 239000010935 stainless steel Substances 0.000 claims description 7
- 239000003054 catalyst Substances 0.000 claims description 5
- 238000004519 manufacturing process Methods 0.000 claims description 5
- 239000000945 filler Substances 0.000 claims description 4
- 238000010438 heat treatment Methods 0.000 claims description 4
- 238000003860 storage Methods 0.000 claims description 4
- 238000001816 cooling Methods 0.000 claims description 3
- 230000005611 electricity Effects 0.000 claims 1
- 238000010586 diagram Methods 0.000 description 7
- 230000000694 effects Effects 0.000 description 7
- 238000000034 method Methods 0.000 description 5
- 238000009303 advanced oxidation process reaction Methods 0.000 description 4
- 230000001105 regulatory effect Effects 0.000 description 4
- 230000009286 beneficial effect Effects 0.000 description 3
- 239000003344 environmental pollutant Substances 0.000 description 3
- 231100000719 pollutant Toxicity 0.000 description 3
- 238000004659 sterilization and disinfection Methods 0.000 description 3
- 230000004048 modification Effects 0.000 description 2
- 238000012986 modification Methods 0.000 description 2
- 230000008569 process Effects 0.000 description 2
- 238000000746 purification Methods 0.000 description 2
- 230000001954 sterilising effect Effects 0.000 description 2
- 230000004075 alteration Effects 0.000 description 1
- 230000003197 catalytic effect Effects 0.000 description 1
- 238000004042 decolorization Methods 0.000 description 1
- 239000003651 drinking water Substances 0.000 description 1
- 235000020188 drinking water Nutrition 0.000 description 1
- 230000002708 enhancing effect Effects 0.000 description 1
- 239000003673 groundwater Substances 0.000 description 1
- 239000010842 industrial wastewater Substances 0.000 description 1
- 230000002085 persistent effect Effects 0.000 description 1
- 239000002957 persistent organic pollutant Substances 0.000 description 1
- 230000009467 reduction Effects 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 231100000331 toxic Toxicity 0.000 description 1
- 230000002588 toxic effect Effects 0.000 description 1
- 238000009736 wetting Methods 0.000 description 1
Landscapes
- Treatment Of Water By Oxidation Or Reduction (AREA)
- Physical Water Treatments (AREA)
Abstract
The utility model provides novel container type ozone advanced oxidation water treatment equipment, which comprises the following components: the device comprises an oxygen preparation system, an ozone preparation system, a high-efficiency gas dissolving system, an ozone contact reaction tank and a tail gas damage system, wherein the oxygen preparation system, the ozone preparation system, the high-efficiency gas dissolving system and the ozone contact reaction tank are sequentially communicated, sewage and ozone are subjected to mixed treatment in the ozone contact reaction tank, and the tail gas damage system is communicated with the ozone contact reaction tank and is used for catalytically treating ozone tail gas. The utility model aims to provide novel container type ozone advanced oxidation water treatment equipment which is used for solving the problems in the prior art.
Description
Technical Field
The utility model relates to the technical field of water treatment equipment, in particular to novel container type ozone advanced oxidation water treatment equipment.
Background
In recent years, the requirements of people on the environment are higher and higher, and the attention to the water environment pollution problem in the process is also higher and higher. In the water environment pollution treatment, the traditional biological treatment process has good treatment effect, but is difficult to meet higher standards, especially for high-concentration industrial wastewater, organic pollutants which are difficult to degrade, persistent toxic trace substances in groundwater or drinking water and the like, the treatment difficulty is increased, compared with the advanced oxidation method, the advanced oxidation method can better remove the pollutants, the water treatment is carried out by utilizing the strong oxidation capability of ozone, meanwhile, the reduction product of the reaction is water, no new pollution is introduced in theory, no selectivity is caused to the pollutants, the pollutants in the complex component water can be better removed, and the advanced oxidation process has the functions of sterilization, disinfection, color removal, odor removal and the like, so that the advanced oxidation process is widely applied in the water treatment industry.
However, the above-described technique has the following drawbacks in specific use: 1. the conventional ozone water treatment equipment is complex, and is troublesome to operate and maintain; 2. existing laboratory-level advanced oxidation process equipment, but lacks container-type and modularized advanced oxidation standard equipment; 3. the integrated equipment which can simultaneously have three advanced oxidation processes of ozone, hydrogen peroxide and ultraviolet is lacking, and flexible combined operation is realized; 4. the automation level is low, the operation of the contact reaction tank is single, and the treatment requirements of the advanced oxidation of different water bodies cannot be met at the same time; 5. the lack of a complete treatment system, especially ozone tail gas treatment, has the problem of safe operation such as catalyst wetting or water inlet failure.
Disclosure of Invention
The utility model provides novel container type ozone advanced oxidation water treatment equipment which is used for solving the problems in the background technology.
Therefore, the technical scheme adopted is that the novel container type ozone advanced oxidation water treatment equipment comprises: the device comprises an oxygen preparation system, an ozone preparation system, a high-efficiency gas dissolving system, an ozone contact reaction tank and a tail gas damage system, wherein the oxygen preparation system, the ozone preparation system, the high-efficiency gas dissolving system and the ozone contact reaction tank are sequentially communicated, sewage and ozone are subjected to mixed treatment in the ozone contact reaction tank, and the tail gas damage system is communicated with the ozone contact reaction tank and is used for catalytically treating ozone tail gas.
Preferably, the automatic control device further comprises a tubular ultraviolet system, wherein the tubular ultraviolet system is automatically controlled through an automatic valve, an ultraviolet sensor is further arranged on the tubular ultraviolet system, and the ultraviolet sensor is connected with the automatic valve to achieve automatic control.
Preferably, the oxygen production system includes: the device comprises an air compressor, a dryer, an air storage tank, an oxygenerator and an oxygen buffer tank which are sequentially connected, wherein a filter is further arranged between the air compressor and the dryer.
Preferably, the ozone production system includes: the ozone generator is communicated with the oxygen buffer tank, the ozone generator is communicated with the air cooler, the air cooler is used for cooling a discharge tube, an electric regulating valve is further arranged at the air outlet end of the ozone generator, an ozone concentration meter, a volume flowmeter and a pressure sensor are further arranged on the ozone generator, and the ozone concentration meter, the volume flowmeter and the pressure sensor are respectively and electrically connected with the electric regulating valve.
Preferably, the high-efficiency gas dissolving system comprises: the efficient dissolved gas system comprises a booster pump, a water injector and a pipeline mixer, wherein the booster pump is connected with the water injector, and the efficient dissolved gas system is also connected with a hydrogen peroxide dosing system.
Preferably, the exhaust gas destruction system includes: the device comprises a steam-water separation tank, a liquid level sensor, a liquid level switch and an electromagnetic valve, wherein the electromagnetic valve is arranged at the bottom of the steam-water separation tank, and the steam-water separation tank is electrically connected with the liquid level sensor and the liquid level switch respectively; the device also comprises a tail breaker, wherein the tail breaker comprises a stainless steel tank body, a heating rod and a filler catalyst, and the rear end of the stainless steel tank body is also connected with an ozone concentration meter.
Preferably, the tubular ultraviolet system further comprises a self-cleaning device, the self-cleaning device comprising:
the liquid inlet pipe and the liquid outlet pipe are respectively connected to the side wall of the pipe body, the axis of the liquid inlet pipe is perpendicular to the axis of the pipe body, and the bottom wall of the pipe body is connected with the control box;
the ultraviolet lamp tube is internally provided with a plurality of ultraviolet lamp tubes along the axial direction, and the ultraviolet lamp tubes are communicated with the control box;
the guide rod is further arranged on the pipe body along the axial direction, one end of the guide rod is fixedly connected with the inner wall of the pipe body, a cleaning sheet is arranged on the guide rod in a sliding mode, the cleaning sheet is arranged to be of a hole net structure, and the ultraviolet lamp tube penetrates through the cleaning sheet and is in sliding connection with the cleaning sheet.
Preferably, the self-cleaning apparatus further comprises: the cleaning device comprises a driving slide block and a driving spring, wherein the guiding rod is of a hollow structure, the driving slide block is arranged in the guiding rod in a sliding mode, the driving spring is arranged between the driving slide block and the end portion of the guiding rod, the axis of the driving spring is consistent with the axis of the guiding rod, a notch is formed in the side wall of the guiding rod along the axial direction, and the driving slide block is connected with a cleaning sheet through the notch.
Preferably, an elastic protection ring is arranged at the joint of the cleaning sheet and the ultraviolet lamp tube, and the elastic protection ring is fixedly connected with the cleaning sheet.
Preferably, the end part of the guide rod is fixedly provided with an anti-falling ball.
The working principle and the beneficial technical effects of the utility model are as follows: the preparation and the contact purification process of ozone are completed through the oxygen preparation system, the ozone preparation system, the efficient gas dissolving system and the ozone contact reaction tank which are sequentially arranged, all the components are arranged in a modularized mode, the components can be combined to be used as required during use, and the ozone tail gas can be treated through the arrangement of the tail gas damage system, so that pollution caused by tail gas is avoided.
Additional features and advantages of the utility model will be set forth in the description which follows, and in part will be obvious from the description, or may be learned by practice of the utility model. The objectives and other advantages of the utility model may be realized and attained by the structure particularly pointed out in the written description and drawings.
The technical scheme of the utility model is further described in detail through the drawings and the embodiments.
Drawings
The accompanying drawings are included to provide a further understanding of the utility model and are incorporated in and constitute a part of this specification, illustrate the utility model and together with the embodiments of the utility model, serve to explain the utility model. In the drawings:
FIG. 1 is a schematic diagram of a novel container-type advanced ozone oxidation water treatment device in an embodiment of the utility model;
FIG. 2 is a schematic diagram II of a novel container-type advanced ozone oxidation water treatment device in an embodiment of the utility model;
FIG. 3 is a schematic diagram III of a novel container-type ozone advanced oxidation water treatment device in an embodiment of the utility model;
FIG. 4 is a schematic diagram of a tail gas destruction system in a novel container-type ozone advanced oxidation water treatment device according to an embodiment of the utility model;
FIG. 5 is a schematic diagram of a self-cleaning device in a novel container-type ozone advanced oxidation water treatment device in an embodiment of the utility model;
FIG. 6 is a schematic diagram II of a self-cleaning device in a novel container-type ozone advanced oxidation water treatment device in an embodiment of the utility model;
fig. 7 is a schematic diagram of a self-cleaning device in a novel container-type ozone advanced oxidation water treatment device in the embodiment of the utility model.
The labels in the figures are as follows: 100. an oxygen production system; 101. an air compressor; 102. a suction drier; 103. an air storage tank; 104. an oxygenerator; 105. an oxygen buffer tank; 200. an ozone preparation system; 201. an ozone generator; 202. an air cooler; 300. an efficient gas dissolving system; 301. a booster pump; 302. a mixer; 400. ozone contacts the reaction tank; 500. a tubular ultraviolet system; 501. a self-cleaning device; 502. a tube body; 503. a liquid inlet pipe; 504. a liquid outlet pipe; 505. a control box; 506. an ultraviolet lamp tube; 507. a guide rod; 508. a cleaning sheet; 509. driving a sliding block; 510. a drive spring; 511. a notch; 512. an elastic protection ring; 513. anti-falling ball; 600. a hydrogen peroxide dosing system; 700. a tail gas destruction system; 710. a steam-water separation tank; 720. a heating rod; 730. a stainless steel tank; 740. a filler catalyst; 750. a liquid level switch; 760. a liquid level sensor; 770. an ozone concentration meter; 780. a bottom solenoid valve.
Detailed Description
The preferred embodiments of the present utility model will be described below with reference to the accompanying drawings, it being understood that the preferred embodiments described herein are for illustration and explanation of the present utility model only, and are not intended to limit the present utility model.
The embodiment of the utility model provides novel container type ozone advanced oxidation water treatment equipment, as shown in figures 1-4, an oxygen preparation system 100, an ozone preparation system 200, a high-efficiency gas dissolving system 300, an ozone contact reaction tank 400 and a tail gas destruction system 700, wherein the oxygen preparation system 100, the ozone preparation system 200, the high-efficiency gas dissolving system 300 and the ozone contact reaction tank 400 are sequentially communicated, sewage and ozone are subjected to mixed treatment in the ozone contact reaction tank 400, and the tail gas destruction system 700 is communicated with the ozone contact reaction tank 400 for catalytic treatment of ozone tail gas;
the automatic control system also comprises a tubular ultraviolet system 500, wherein the tubular ultraviolet system 500 realizes automatic control through an automatic valve, and an ultraviolet sensor is also arranged on the tubular ultraviolet system 500 and is connected with the automatic valve to realize automatic control;
the oxygen production system 100 includes: the device comprises an air compressor 101, a dryer 102, an air storage tank 103, an oxygen generator 104 and an oxygen buffer tank 105 which are sequentially connected, wherein a filter is further arranged between the air compressor 101 and the dryer 102;
the ozone generating system 200 includes: the ozone generator 201 is communicated with the oxygen buffer tank 105, the ozone generator 201 is communicated with the air cooler 202, the air cooler 202 is used for cooling a discharge tube, an electric regulating valve is further arranged at the air outlet end of the ozone generator 201, an ozone concentration meter 770, a volume flowmeter and a pressure sensor are further arranged on the ozone generator 201, and the ozone concentration meter 770, the volume flowmeter and the pressure sensor are respectively and electrically connected with the electric regulating valve;
the high efficiency gas dissolving system 300 includes: the efficient dissolved gas system comprises a booster pump 301, a water injector and a pipeline mixer 302, wherein the booster pump 301 is connected with the water injector, and the efficient dissolved gas system is also connected with a hydrogen peroxide dosing system;
the exhaust gas destruction system 700 includes: the steam-water separation tank 710, the liquid level sensor 760, the liquid level switch 750 and the electromagnetic valve, wherein the electromagnetic valve is arranged at the bottom of the steam-water separation tank 710, and the steam-water separation tank 710 is electrically connected with the liquid level sensor 760 and the liquid level switch 750 respectively; the device also comprises a tail breaker, wherein the tail breaker comprises a stainless steel tank body 730, a heating rod 720 and a filler catalyst 740, and the tail of the stainless steel tank body 730 is also connected with an ozone concentration meter 770.
The technical scheme has the working principle and beneficial technical effects that: the preparation and the contact purification process of ozone are completed through the oxygen preparation system 100, the ozone preparation system 200, the high-efficiency gas dissolving system 300 and the ozone contact reaction tank 400 which are sequentially arranged, all the components are arranged in a modularized mode, the components can be combined to be used as required during use, and the tail gas destruction system 700 can treat ozone tail gas to avoid pollution caused by the tail gas.
In one embodiment, as shown in fig. 5-7, the tubular ultraviolet system 500 further comprises a self-cleaning device 501, the self-cleaning device 501 comprising:
the pipe body 502 is arranged in a cylindrical shape, the axis of the pipe body 502 is horizontally arranged, two ends of the pipe body 502 are closed, a liquid inlet pipe 503 and a liquid outlet pipe 504 are respectively connected to the side wall of the pipe body 502, the axis of the liquid inlet pipe 503 is perpendicular to the axis of the pipe body 502, and a control box 505 is connected to the bottom wall of the pipe body 502;
an ultraviolet lamp 506, a plurality of ultraviolet lamps 506 are arranged in the tube body 502 along the axial direction, and the ultraviolet lamp 506 is communicated with the control box 505;
the guide rod 507, the tube body 502 is further provided with a guide rod 507 along the axial direction, one end of the guide rod 507 is fixedly connected with the inner wall of the tube body 502, the guide rod 507 is provided with a cleaning sheet 508 in a sliding manner, the cleaning sheet 508 is provided with a hole net structure, and the ultraviolet lamp 506 passes through the cleaning sheet 508 and is connected with the cleaning sheet 508 in a sliding manner;
the self-cleaning apparatus 501 further comprises: the guide rod 507 is provided with a hollow structure, the guide rod 507 is slidably provided with the guide rod 509, a drive spring 510 is arranged between the guide rod 507 and the end part of the guide rod 507, the axis of the drive spring 510 is consistent with that of the guide rod 507, a notch 511 is formed in the side wall of the guide rod 507 along the axial direction, and the guide rod 509 is connected with the cleaning sheet 508 through the notch 511;
an elastic protection ring 512 is arranged at the joint of the cleaning sheet 508 and the ultraviolet lamp 506, and the elastic protection ring 512 is fixedly connected with the cleaning sheet 508;
the end of the guide rod 507 is fixedly provided with an anti-falling ball 513.
The technical scheme has the working principle and beneficial technical effects that: when the self-cleaning device 501 is in use, liquid enters the tube body 502 along the liquid inlet pipe 503, and at this time, the liquid is sterilized and disinfected in the tube body 502 through the ultraviolet lamp 506. The cleaning sheet 508 is pushed when the liquid flows along the tube body 502, and the residual condensate on the ultraviolet lamp 506 is scraped off when the cleaning sheet 508 moves, so that the cleaning effect is achieved, and meanwhile, the elastic protection ring 512 can prevent the ultraviolet lamp 506 from being damaged, can increase friction force and improves the cleaning effect on the ultraviolet lamp 506; further, the provision of the cleaning sheet 508 also increases the residence time of the liquid within the tube 502, thereby further enhancing the sterilization effect.
It will be apparent to those skilled in the art that various modifications and variations can be made to the present utility model without departing from the spirit or scope of the utility model. Thus, it is intended that the present utility model also include such modifications and alterations insofar as they come within the scope of the appended claims or the equivalents thereof.
Claims (10)
1. Novel container formula ozone advanced oxidation water treatment facilities, its characterized in that includes: the device comprises an oxygen preparation system (100), an ozone preparation system (200), a high-efficiency gas dissolving system (300), an ozone contact reaction tank (400) and a tail gas destruction system (700), wherein the oxygen preparation system (100), the ozone preparation system (200), the high-efficiency gas dissolving system (300) and the ozone contact reaction tank (400) are sequentially communicated, sewage and ozone are subjected to mixed treatment in the ozone contact reaction tank (400), and the tail gas destruction system (700) is communicated with the ozone contact reaction tank (400) and is used for catalytically treating ozone tail gas.
2. The novel container type ozone advanced oxidation water treatment device according to claim 1, further comprising a tubular ultraviolet system (500), wherein the tubular ultraviolet system (500) is automatically controlled through an automatic valve, an ultraviolet sensor is further arranged on the tubular ultraviolet system (500), and the ultraviolet sensor is connected with the automatic valve to achieve automatic control.
3. A new container-type ozone advanced oxidation water treatment device according to claim 1, characterized in that the oxygen production system (100) comprises: the device comprises an air compressor (101), a dryer (102), an air storage tank (103), an oxygenerator (104) and an oxygen buffer tank (105) which are sequentially connected, wherein a filter is further arranged between the air compressor (101) and the dryer (102).
4. A new container-type ozone advanced oxidation water treatment device according to claim 1, characterized in that the ozone preparation system (200) comprises: ozone generator (201) and air cooler (202), ozone generator (201) and oxygen buffer tank (105) intercommunication, ozone generator (201) and air cooler (202) intercommunication, air cooler (202) are used for the discharge tube cooling, ozone generator (201) is given vent to anger the end and is still provided with electric control valve, ozone generator (201) are last still to be provided with ozone concentration meter (770), volumetric flowmeter and pressure sensor, ozone concentration meter (770), volumetric flowmeter and pressure sensor are connected with electric control valve electricity respectively.
5. A new container-type ozone advanced oxidation water treatment device according to claim 1, characterized in that the efficient dissolved air system (300) comprises: the hydrogen peroxide dosing system comprises a booster pump (301), a water injector and a pipeline mixer (302), wherein the booster pump (301) is connected with the water injector, and the high-efficiency gas dissolving system (300) is further connected with the hydrogen peroxide dosing system (600).
6. A new container-type ozone advanced oxidation water treatment device according to claim 5, characterized in that the tail gas destruction system (700) comprises: the device comprises a steam-water separation tank (710), a liquid level sensor (760), a liquid level switch (750) and an electromagnetic valve, wherein the electromagnetic valve is arranged at the bottom of the steam-water separation tank (710), and the steam-water separation tank (710) is electrically connected with the liquid level sensor (760) and the liquid level switch (750) respectively; the device also comprises a tail breaker, wherein the tail breaker comprises a stainless steel tank body (730), a heating rod (720) and a filler catalyst (740), and the rear end of the stainless steel tank body (730) is also connected with an ozone concentration meter (770).
7. A new container-type ozone advanced oxidation water treatment device according to claim 2, characterized in that the tubular ultraviolet system (500) further comprises a self-cleaning device (501), the self-cleaning device (501) comprising:
the liquid inlet pipe comprises a pipe body (502), wherein the pipe body (502) is arranged in a cylindrical shape, the axis of the pipe body (502) is arranged horizontally, two ends of the pipe body (502) are closed, a liquid inlet pipe (503) and a liquid outlet pipe (504) are respectively connected to the side wall of the pipe body (502), the axis of the liquid inlet pipe (503) is perpendicular to the axis of the pipe body (502), and a control box (505) is connected to the bottom wall of the pipe body (502);
the ultraviolet lamp tube (506) is arranged in the tube body (502) along the axial direction, and the ultraviolet lamp tube (506) is communicated with the control box (505);
guide rod (507), body (502) still are provided with guide rod (507) along the axial, belonged guide rod (507) one end with body (502) inner wall fixed connection, slide on guide rod (507) and be provided with cleaning sheet (508), cleaning sheet (508) set up to the hole net structure, ultraviolet fluorescent tube (506) pass cleaning sheet (508) and with cleaning sheet (508) sliding connection.
8. A new container-type ozone advanced oxidation water treatment device according to claim 7, characterized in that the self-cleaning device (501) further comprises: the cleaning device comprises a driving sliding block (509) and a driving spring (510), wherein the guiding rod (507) is of a hollow structure, the driving sliding block (509) is arranged in the guiding rod (507), the driving spring (510) is arranged between the driving sliding block (509) and the end part of the guiding rod (507), the axis of the driving spring (510) is consistent with that of the guiding rod (507), a notch (511) is formed in the side wall of the guiding rod (507) along the axial direction, and the driving sliding block (509) is connected with a cleaning sheet (508) through the notch (511).
9. The novel container-type advanced ozone oxidation water treatment device according to claim 7, wherein an elastic protection ring (512) is arranged at the joint of the cleaning sheet (508) and the ultraviolet lamp tube (506), and the elastic protection ring (512) is fixedly connected with the cleaning sheet (508).
10. The novel container type ozone advanced oxidation water treatment equipment according to claim 7, wherein the end part of the guide rod (507) is fixedly provided with an anti-falling ball (513).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202322112842.3U CN220537586U (en) | 2023-08-08 | 2023-08-08 | Novel container type ozone advanced oxidation water treatment equipment |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202322112842.3U CN220537586U (en) | 2023-08-08 | 2023-08-08 | Novel container type ozone advanced oxidation water treatment equipment |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN220537586U true CN220537586U (en) | 2024-02-27 |
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ID=89960340
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN202322112842.3U Active CN220537586U (en) | 2023-08-08 | 2023-08-08 | Novel container type ozone advanced oxidation water treatment equipment |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN220537586U (en) |
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2023
- 2023-08-08 CN CN202322112842.3U patent/CN220537586U/en active Active
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