CN204675939U - The system of a kind of ultraviolet and ozone hydrogen peroxide interlock process industry and sanitary wastewater - Google Patents
The system of a kind of ultraviolet and ozone hydrogen peroxide interlock process industry and sanitary wastewater Download PDFInfo
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- CN204675939U CN204675939U CN201520378576.1U CN201520378576U CN204675939U CN 204675939 U CN204675939 U CN 204675939U CN 201520378576 U CN201520378576 U CN 201520378576U CN 204675939 U CN204675939 U CN 204675939U
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Abstract
The system of a kind of ultraviolet and ozone hydrogen peroxide interlock process industry and sanitary wastewater, reactor offers water-in and water outlet, the water outlet of hydrogen peroxide supply pool and the water outlet of waste water transport pipe all with the inlet communication of static mixer, the outlet of static mixer is communicated with the water-in of reactor, be provided with multiple ozone sparger and multiple quartz burner in reactor, the import of ozone sparger all with the outlet of ozonizer.Processing efficiency is high, good purification, generally completes within one second the germicidal action of bacterium, virus, germ-killing efficiency is high, and high-level efficiency can kill most of pathogenic protozoa, bacterium, virus, more particularly endangers comparatively greatly the mankind and has the protozoa of oxidation-resistance, secondary pollution can not be produced to water body and surrounding environment, also can not etching apparatus, structure is simple, easy to operate, safe and reliable to operation, floor space is little, and running maintenance is simple, and expense is low.
Description
Technical field
The utility model belongs to technical field of sewage treatment equipment, relates to the system of a kind of ultraviolet and ozone hydrogen peroxide interlock process industry and sanitary wastewater.
Background technology
Along with the fast development of basic industry, water pollution is day by day serious, and Available water resources constantly reduces, and people more and more pay attention to the application of sewage reuse techuique.Concentrating of industrial expansion and population, makes constantly to increase from the sanitary sewage amount of family, office, business and urban public utilities and contained pollutant kind, wherein mainly ight soil and wash water.These sewage to enter after water body often communicate illness, and can cause Suspended Matter in Water quantity and biological oxygen demand more and more higher, water hypoxia, hydrobiont becomes extinct.Along with people get more and more to the demand of water, after sewage disposal, reuse becomes the effective way solving shortage of water resources problem.
Summary of the invention
The utility model is in order to overcome the defect of prior art, devise the system of a kind of ultraviolet and ozone hydrogen peroxide interlock process industry and sanitary wastewater, can taste removal, decolouring, improve water quality, germ-killing efficiency is high, and processing efficiency is high, good purification, structure is simple, easy to operate, floor space is little, can meet the demand of people to wastewater ocean disposal.
The concrete technical scheme that the utility model is taked is: the system of a kind of ultraviolet and ozone hydrogen peroxide interlock process industry and sanitary wastewater, comprise waste water transport pipe, key is: described system also comprises hydrogen peroxide supply pool, static mixer, ozonizer and reactor, reactor offers water-in and water outlet, the water outlet of hydrogen peroxide supply pool and the water outlet of waste water transport pipe all with the inlet communication of static mixer, the outlet of static mixer is communicated with the water-in of reactor, multiple ozone sparger and multiple quartz burner is provided with in reactor, the import of ozone sparger all with the outlet of ozonizer.
Described system also comprises Ozone Absorption device, and the top of reactor offers air outlet, and the import of Ozone Absorption device is communicated with the air outlet of reactor.
Described reactor is rectangular vessel, the division plate of multiple vertical setting is provided with in reactor, all division plates are arranged at equal intervals along the length direction of reactor, the reaction chamber that inside reactor becomes multiple top to be communicated with by divides, the water-in of reactor is arranged on the bottom of a width sidewall, and the water outlet of reactor is arranged on the bottom of another width sidewall.
Be provided with at least one ozone sparger in described each reaction chamber, ozone sparger is positioned at the bottom of reaction chamber.
Be provided with the quartz burner of equal amount in described each reaction chamber, all quartz burners all vertically arrange and arrange at equal intervals in the width direction.
Four quartz burners are provided with in described each reaction chamber.
The power of described quartz burner is 65W.
The beneficial effects of the utility model are: utilize ultraviolet simultaneously, ozone and hydrogen peroxide process industry and sanitary wastewater, processing efficiency is high, good purification, to various germ, bacterium all has very strong kills ability, energy taste removal, decolouring, improve water quality, to bacterium, the germicidal action of virus generally completed within one second, germ-killing efficiency is high, and high-level efficiency can kill most of pathogenic protozoa, bacterium, virus, more particularly the mankind endangered comparatively greatly and have the protozoa of oxidation-resistance, as Cryptosporidium and giardia lamblia stiles etc., owing to not adding any chemical agent, so secondary pollution can not be produced to water body and surrounding environment, can be directly carbonic acid gas and water by pollutant oxidation, also can not etching apparatus, structure is simple, easy to operate, safe and reliable to operation, floor space is little, running maintenance is simple, expense is low, the demand of people to wastewater ocean disposal can be met.
Accompanying drawing explanation
Fig. 1 is structural representation of the present utility model.
In accompanying drawing, 1 represents ozonizer, and 2 represent Ozone Absorption device, and 3 represent ozone sparger, and 4 represent hydrogen peroxide supply pool, and 5 represent static mixer, and 6 represent reactor, and 7 represent quartz burner.
Embodiment
Below in conjunction with the drawings and specific embodiments, the utility model is elaborated:
Specific embodiment, as shown in Figure 1, the system of a kind of ultraviolet and ozone hydrogen peroxide interlock process industry and sanitary wastewater, comprise waste water transport pipe, also comprise hydrogen peroxide supply pool 4, static mixer 5, ozonizer 1 and reactor 6, reactor 6 offers water-in and water outlet, the water outlet of hydrogen peroxide supply pool 4 and the water outlet of waste water transport pipe all with the inlet communication of static mixer 5, the outlet of static mixer 5 is communicated with the water-in of reactor 6, multiple ozone sparger 3 and multiple quartz burner 7 is provided with in reactor 6, the power of quartz burner 7 is 65W, it is ultraviolet in 254nm and neighbouring wavelength region thereof that quartz burner 7 gives out wavelength, ultraviolet makes the base pair of microbial DNA be polymerized, stop protein synthesis and make microorganism irreproducible, there is broad-spectrum bactericidal capacity, it is the sterilization method that uniquely can not produce disinfection byproduct (DBP), the import of ozone sparger 3 all with the outlet of ozonizer 1.Ozone is internationally recognized environmental type disinfection sanitizer, disinfection efficiency is high, all have various virus, bacterium and very strong kill ability, it can also taste removal, decolouring, improve water quality, and there is no secondary pollution, ozone/hydrogen peroxide is a kind of important advanced oxidization method in water treatment, and it does not produce secondary pollution, can be directly carbonic acid gas and water by pollutant oxidation, this linked system processing efficiency is high, good purification, structure is simple, easy to operate, floor space is little, can meet the demand of people to wastewater ocean disposal.
As to further improvement of the utility model, system also comprises Ozone Absorption device 2, the top of reactor 6 offers air outlet, the import of Ozone Absorption device 2 is communicated with the air outlet of reactor 6, not having the ozone dissolved to be relatively unabsorbed by ozone device 2 sorption enhanced in reactor 6 is oxygen, and ozone is fully utilized.
As to further improvement of the utility model, reactor 6 is rectangular vessel, the division plate of multiple vertical setting is provided with in reactor 6, all division plates are arranged at equal intervals along the length direction of reactor 6, the reaction chamber that reactor 6 inside becomes multiple top to be communicated with by divides, the water-in of reactor 6 is arranged on the bottom of a width sidewall, the water outlet of reactor 6 is arranged on the bottom of another width sidewall, sewage is discharged by water outlet after entering from water-in successively after each reaction chamber, the time that sewage is cleaned can be extended like this, improve decontamination effect improving.Be provided with at least one ozone sparger 3 in each reaction chamber, ozone sparger 3 is positioned at the bottom of reaction chamber, can improve the dissolved efficiency of ozone, and ozone is distributed more even, abundant and waste water, improves decontamination effect improving.Be provided with the quartz burner 7 of equal amount in each reaction chamber, be preferably four, all quartz burners 7 all vertically arrange and arrange at equal intervals in the width direction, irradiate evenly, good purification.
The utility model is in the specific implementation: waste water is when entering static mixer 5 by waste water transport pipe, hydrogen peroxide in hydrogen peroxide supply pool 4 also enters static mixer 5, both mixing contacts, then reactor 6 is flow to certain speed, the ozone that ozonizer 1 produces is distributed in each reaction chamber through ozone sparger 3, sewage and ultraviolet and ozone contact, when in ozone solution to waste water, hydroxyl just creates, the ultraviolet that this process is sent by quartz burner 7 and the catalysis of hydrogen peroxide institute, there is no the ozone dissolved before being discharged to air, first by Ozone Absorption device 2, Ozone Absorption device 2 uses special nickel catalyzator that ozone waste gas is converted into oxygen, its maximum throughput can reach 900Nm
3/ min, can be reduced to below 0.1mg/L by the ozone concn in 1 ~ 20000mg/L, ozone can be made to be fully used.
Claims (7)
1. the system of a ultraviolet and ozone hydrogen peroxide interlock process industry and sanitary wastewater, comprise waste water transport pipe, it is characterized in that: described system also comprises hydrogen peroxide supply pool (4), static mixer (5), ozonizer (1) and reactor (6), (6) offer water-in and water outlet to reactor, the water outlet of hydrogen peroxide supply pool (4) and the water outlet of waste water transport pipe all with the inlet communication of static mixer (5), the outlet of static mixer (5) is communicated with the water-in of reactor (6), multiple ozone spargers (3) and multiple quartz burner (7) is provided with in reactor (6), the import of ozone sparger (3) all with the outlet of ozonizer (1).
2. the system of a kind of ultraviolet and ozone hydrogen peroxide interlock process industry according to claim 1 and sanitary wastewater, it is characterized in that: described system also comprises Ozone Absorption device (2), the top of reactor (6) offers air outlet, and the import of Ozone Absorption device (2) is communicated with the air outlet of reactor (6).
3. the system of a kind of ultraviolet and ozone hydrogen peroxide interlock process industry according to claim 1 and sanitary wastewater, it is characterized in that: described reactor (6) is rectangular vessel, the division plate of multiple vertical setting is provided with in reactor (6), all division plates are arranged at equal intervals along the length direction of reactor (6), the reaction chamber that reactor (6) inside becomes multiple top to be communicated with by divides, the water-in of reactor (6) is arranged on the bottom of a width sidewall, the water outlet of reactor (6) is arranged on the bottom of another width sidewall.
4. the system of a kind of ultraviolet and ozone hydrogen peroxide interlock process industry according to claim 3 and sanitary wastewater, it is characterized in that: be provided with at least one ozone sparger (3) in described each reaction chamber, ozone sparger (3) is positioned at the bottom of reaction chamber.
5. the system of a kind of ultraviolet and ozone hydrogen peroxide interlock process industry according to claim 3 and sanitary wastewater, it is characterized in that: the quartz burner (7) being provided with equal amount in described each reaction chamber, all quartz burners (7) all vertically arrange and arrange at equal intervals in the width direction.
6. a kind of ultraviolet and ozone hydrogen peroxide interlock process industry according to claim 5 and the system of sanitary wastewater, is characterized in that: be provided with four quartz burners (7) in described each reaction chamber.
7. a kind of ultraviolet and ozone hydrogen peroxide interlock process industry according to claim 1 and the system of sanitary wastewater, is characterized in that: the power of described quartz burner (7) is 65W.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520378576.1U CN204675939U (en) | 2015-06-04 | 2015-06-04 | The system of a kind of ultraviolet and ozone hydrogen peroxide interlock process industry and sanitary wastewater |
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| Application Number | Priority Date | Filing Date | Title |
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| CN201520378576.1U CN204675939U (en) | 2015-06-04 | 2015-06-04 | The system of a kind of ultraviolet and ozone hydrogen peroxide interlock process industry and sanitary wastewater |
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| CN201520378576.1U Expired - Fee Related CN204675939U (en) | 2015-06-04 | 2015-06-04 | The system of a kind of ultraviolet and ozone hydrogen peroxide interlock process industry and sanitary wastewater |
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Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107098433A (en) * | 2017-06-26 | 2017-08-29 | 深圳清华大学研究院 | Water body disinfection system and vertical non-pressure ultraviolet radiation for water body disinfecting reactor |
| CN107986545A (en) * | 2018-01-22 | 2018-05-04 | 过嘉明 | Haemodialysis control unit wastewater treatment equipment |
| CN110339666A (en) * | 2019-08-12 | 2019-10-18 | 中国科学院城市环境研究所 | A kind of method that ozone generates concentration in lift gas |
| CN113860603A (en) * | 2021-10-13 | 2021-12-31 | 福建师范大学 | Sweet potato wastewater treatment method |
-
2015
- 2015-06-04 CN CN201520378576.1U patent/CN204675939U/en not_active Expired - Fee Related
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107098433A (en) * | 2017-06-26 | 2017-08-29 | 深圳清华大学研究院 | Water body disinfection system and vertical non-pressure ultraviolet radiation for water body disinfecting reactor |
| CN107986545A (en) * | 2018-01-22 | 2018-05-04 | 过嘉明 | Haemodialysis control unit wastewater treatment equipment |
| CN110339666A (en) * | 2019-08-12 | 2019-10-18 | 中国科学院城市环境研究所 | A kind of method that ozone generates concentration in lift gas |
| CN113860603A (en) * | 2021-10-13 | 2021-12-31 | 福建师范大学 | Sweet potato wastewater treatment method |
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| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20150930 |