CN204022606U - The super oxidation system of a kind of EPN livestock and poultry cultivation sewage disposal acousto-optic chemistry - Google Patents
The super oxidation system of a kind of EPN livestock and poultry cultivation sewage disposal acousto-optic chemistry Download PDFInfo
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- CN204022606U CN204022606U CN201420451442.3U CN201420451442U CN204022606U CN 204022606 U CN204022606 U CN 204022606U CN 201420451442 U CN201420451442 U CN 201420451442U CN 204022606 U CN204022606 U CN 204022606U
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Abstract
The utility model relates to the super oxidation system of a kind of special chemistry of the EPN livestock and poultry cultivation sewage disposal acousto-optic for livestock and poultry cultivation sewage disposal, by O
3generating unit forms with the ultraviolet catalytic unit being connected with Catalyzed by Ultrasonic Wave unit pipe, and the water intake end in Catalyzed by Ultrasonic Wave unit is provided with ozonizer and pressure pump; Ultraviolet catalytic unit comprises S type runner, ultraviolet source, sewage outlet.The utility model is comprised of ozone, ultrasonic wave, ultraviolet ray, take ozone as catalyzer, making full use of ultrasonic cavitation effect forms advanced oxidation with the hydrogen peroxide synthesis of hydroxy free radical producing in photochemical catalysis and reacts, COD, BOD, ammonia-nitrogen content be can efficiently reduce, and water burning, free-radical oxidn utilized, high temperature pyrolysis, in one, have well sterilization effect widely with supercritical oxidation, the microbiotic of comprehensively removing in breeding wastewater pollutes.
Description
Technical field
The utility model relates to livestock and poultry cultivation sewage treatment area, specifically discloses the super oxidation system of a kind of EPN livestock and poultry cultivation sewage disposal acousto-optic chemistry.
Background technology
Tetracycline antibiotics is as a kind of spectrum antibiotic, worldwide be widely used in the diseases prevention and treatment of livestock and poultry farms in scale animal bacterial infection, owing to thering is highly water-soluble, the feature such as be difficult for degraded in environment and easily accumulate, in livestock breeding wastewater, residual microbiotic can produce huge ecological toxicological effect, because microbiotic has strong restraining effect to bioprocess, conventional livestock and poultry cultivation blowdown treatment technology, in line or the reuse of the general employing of water after processing, but in water body, still contain part ammonia nitrogen, COD, BOD, microbiotic, intestinal bacteria and bacterial micro-organism etc., cause water body rotten between staging life at clean water basin, as water body reddens, bacteria breed, produce stench etc., and antibiotic cannot removal causes the secondary pollution that a large amount of enrichments of surface water microbiotic have caused water body, so that sewage disposal has lost former meaningful.
Utility model content
The purpose of this utility model is improved according to the shortcoming existing in background technology and problem, provides a kind of and can further reduce COD, BOD, ammonia-nitrogen content, has extensive sterilization effect, can effectively remove the super oxidation system of antibiotic EPN livestock and poultry cultivation sewage disposal acousto-optic chemistry.
The technical solution of the utility model is to provide the super oxidation system of a kind of EPN livestock and poultry cultivation sewage disposal acousto-optic chemistry, it is characterized in that being formed with the ultraviolet catalytic unit being connected with Catalyzed by Ultrasonic Wave unit pipe by Catalyzed by Ultrasonic Wave unit, wherein: the water intake end in described Catalyzed by Ultrasonic Wave unit is provided with ozonizer and pressure pump, on the rising pipe of this ozonizer output tube and pressure pump, be provided with ejector; Catalyzed by Ultrasonic Wave unit inner bottom part is provided with for sending hyperacoustic ultrasonic wave shake plate; Described ultraviolet catalytic unit comprises the S type runner that consists of glass flows guidance tape, be disposed on ultraviolet lamp in this S type runner, be arranged on this S type flow field end and be positioned at the sewage outlet on top, ultraviolet catalytic unit; Sewage enters and drains into Catalyzed by Ultrasonic Wave unit by ejector from pressure pump and carries out catalytic ozonation, then drains into the bottom of ultraviolet catalytic unit, and the sewage after Catalyzed by Ultrasonic Wave carries out sterilization by S type runner and under the irradiation of ultraviolet lamp.
The utlity model has following advantage:
The utility model is comprised of ozone, ultrasonic wave, ultraviolet ray, take ozone as catalyzer, making full use of ultrasonic cavitation effect forms advanced oxidation with the hydrogen peroxide synthesis of hydroxy free radical producing in photochemical catalysis and reacts, COD, BOD, ammonia-nitrogen content be can efficiently reduce, and water burning, free-radical oxidn utilized, high temperature pyrolysis, in one, have well sterilization effect widely with supercritical oxidation, the microbiotic of comprehensively removing in breeding wastewater pollutes.
Accompanying drawing explanation
Fig. 1 is the utility model structural representation.
Fig. 2 is the utility model principle flow chart.
Embodiment
From Fig. 1-2, the utility model is comprised of with the ultraviolet catalytic unit 15 being connected with Catalyzed by Ultrasonic Wave unit 14 pipelines Catalyzed by Ultrasonic Wave unit 14, wherein: the water intake end in described Catalyzed by Ultrasonic Wave unit 14 is provided with ozonizer 2 and pressure pump 1, on the rising pipe of these ozonizer 2 output tubes and pressure pump 1, be provided with ejector 3; Catalyzed by Ultrasonic Wave unit 14 inner bottom parts are provided with for sending hyperacoustic ultrasonic wave shake plate 4; Described ultraviolet catalytic unit 15 comprises the S type runner that consists of glass flows guidance tape 10, be disposed on ultraviolet lamp 8 in this S type runner, be arranged on this S type flow field end and be positioned at the sewage outlet 11 on 15 tops, ultraviolet catalytic unit; Sewage enters and drains into Catalyzed by Ultrasonic Wave unit 14 by ejector 3 from pressure pump 1 and carries out catalytic ozonation, drain into the bottom of ultraviolet catalytic unit 15, the sewage after Catalyzed by Ultrasonic Wave carries out sterilization by S type runner and under the equilibrium of ultraviolet lamp 8 is irradiated again.
14 tops, Catalyzed by Ultrasonic Wave described in the utility model unit are provided with tensimeter 6 and automatic decompression valve 7.14 bottoms, Catalyzed by Ultrasonic Wave described in the utility model unit are provided with sewage evacuation port 5.15 tops, ultraviolet catalytic described in the utility model unit are provided with tensimeter 12 and automatic decompression valve 13.15 bottoms, ultraviolet catalytic described in the utility model unit are provided with sewage evacuation port 9.Ultrasonic wave described in the utility model shake plate 4 is different 2 of frequency, is oppositely arranged in Catalyzed by Ultrasonic Wave unit 14.14 bottoms, Catalyzed by Ultrasonic Wave described in the utility model unit are equipped with and are made water body be evenly distributed on the interceptor in casing.
In the super oxidation system of EPN livestock and poultry cultivation sewage disposal acousto-optic chemistry, ozone, ultrasonic wave, ultraviolet ray form advanced oxidation reaction, take ozone as catalyzer, making full use of ultrasonic cavitation effect forms advanced oxidation with the hydrogen peroxide synthesis of hydroxy free radical producing in photochemical catalysis and reacts, can efficiently reduce COD, BOD, ammonia-nitrogen content, and utilize water to burn, free-radical oxidn, high temperature pyrolysis, and supercritical oxidation is in one.Have well sterilization effect widely, the microbiotic of comprehensively removing in breeding wastewater pollutes.
The utility model principle of work:
Sewage enters Catalyzed by Ultrasonic Wave unit 14 by pressure pump 1, in ejector 3, fully mix with ozone, in the catalysis of ultrasound unit catalytic unit, ultrasonic wave shake plate 4 sends 28KHz and 25KHZ ultrasonic wave, under constant output condition, improve reverberation field intensity enhancing cavitation effect, improve ultrasonic radiation area, intensified response efficiency, the high-temperature and high-pressure conditions that ultrasonic cavitation produces is enough to open the chemical bond that bonding force is strong, and promotes " water burning " reaction.In cavitation " focus ", there is the reactions such as chemical bond rupture, water burning, pyrolytic decomposition, supercritical water oxidation, free-radical oxidn in organism.These effects add that the particle vibration in sound field, secondary derivative ripple etc. provide the unapproachable degraded of other water treatment method many organic approach.Ultrasonic cavitation provides an extreme physical environment for chemical reaction, can open up new means of chemical reaction like this, the rapid chemical reaction velocity that increases, organism is had to good degradation capability, general process continues ultrasonication and may ultimately reach permineralization, and ultrasonic wave makes ozone bubbles broken simultaneously, forms atomic small bubbles or dissolving, make ozone oxidation surface-area increase several times, reach best ozone oxidation effect; Sewage through Catalyzed by Ultrasonic Wave enters 15 bottoms, ultraviolet catalytic unit, by S type glass channel 10, through ultraviolet lamp 8 prolonged exposures, finally by sewage outlet, is discharged; Glass flows guidance tape 10 printing opacities are good, and resistance to oxidation forms S type runner and can make sewage irradiate evenly, sufficient reacting; The effect of emptying sewage and sediment exclusion when 5,9 conducts of sewage evacuation port are safeguarded; Tensimeter 6,12 is for display unit internal pressure, and automatic decompression valve 7,13, for relief pressure, is discharged unnecessary gas.Built-in two ultrasonic systems of the utility model, install on opposite, and frequency is different, promotes the reaction of ozone, promotes cavitation effect simultaneously, eliminates to greatest extent the pollutent in sewage.
Embodiment described in the utility model is only the description that preferred implementation of the present utility model is carried out; not the utility model design and scope are limited; do not departing under the prerequisite of the utility model design philosophy; various modification and improvement that in this area, engineering technical personnel make the technical solution of the utility model; all should fall into protection domain of the present utility model; the technology contents that the utility model is asked for protection, is all documented in claims.
Claims (7)
1. the super oxidation system of EPN livestock and poultry cultivation sewage disposal acousto-optic chemistry, is characterized in that being comprised of with the ultraviolet catalytic unit (15) being connected with Catalyzed by Ultrasonic Wave unit (14) pipeline Catalyzed by Ultrasonic Wave unit (14), wherein:
Water intake end in described Catalyzed by Ultrasonic Wave unit (14) is provided with ozonizer (2) and pressure pump (1), on the rising pipe of this ozonizer (2) output tube and pressure pump (1), is provided with ejector (3); Catalyzed by Ultrasonic Wave unit (14) inner bottom part is provided with for sending hyperacoustic ultrasonic wave shake plate (4);
Described ultraviolet catalytic unit (15) comprises the S type runner that consists of glass flows guidance tape (10), be disposed on ultraviolet lamp (8) in this S type runner, be arranged on this S type flow field end and be positioned at the sewage outlet (11) on top, ultraviolet catalytic unit (15);
Sewage enters and passes through ejector (3) from pressure pump (1) and drains into Catalyzed by Ultrasonic Wave unit (14) and carry out catalytic ozonation, drain into the bottom of ultraviolet catalytic unit (15), the sewage after Catalyzed by Ultrasonic Wave carries out sterilization by S type runner and under the irradiation of ultraviolet lamp (8) again.
2. the super oxidation system of a kind of EPN livestock and poultry cultivation sewage disposal acousto-optic chemistry according to claim 1, is characterized in that: described top, Catalyzed by Ultrasonic Wave unit (14) is provided with tensimeter (6) and automatic decompression valve (7).
3. the super oxidation system of a kind of EPN livestock and poultry cultivation sewage disposal acousto-optic chemistry according to claim 1, is characterized in that: described bottom, Catalyzed by Ultrasonic Wave unit (14) is provided with sewage evacuation port (5).
4. the super oxidation system of a kind of EPN livestock and poultry cultivation sewage disposal acousto-optic chemistry according to claim 1, is characterized in that: described top, ultraviolet catalytic unit (15) is provided with tensimeter (12) and automatic decompression valve (13).
5. the super oxidation system of a kind of EPN livestock and poultry cultivation sewage disposal acousto-optic chemistry according to claim 1, is characterized in that: described bottom, ultraviolet catalytic unit (15) is provided with sewage evacuation port (9).
6. the super oxidation system of a kind of EPN livestock and poultry cultivation sewage disposal acousto-optic chemistry according to claim 1, is characterized in that: described ultrasonic wave shake plate (4), for different 2 of frequency, is oppositely arranged in Catalyzed by Ultrasonic Wave unit (14).
7. the super oxidation system of a kind of EPN livestock and poultry cultivation sewage disposal acousto-optic chemistry according to claim 1, is characterized in that: described bottom, Catalyzed by Ultrasonic Wave unit (14) is equipped with and is made water body be evenly distributed on the interceptor in casing.
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| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201420451442.3U CN204022606U (en) | 2014-08-12 | 2014-08-12 | The super oxidation system of a kind of EPN livestock and poultry cultivation sewage disposal acousto-optic chemistry |
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| CN201420451442.3U CN204022606U (en) | 2014-08-12 | 2014-08-12 | The super oxidation system of a kind of EPN livestock and poultry cultivation sewage disposal acousto-optic chemistry |
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| CN201420451442.3U Expired - Fee Related CN204022606U (en) | 2014-08-12 | 2014-08-12 | The super oxidation system of a kind of EPN livestock and poultry cultivation sewage disposal acousto-optic chemistry |
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Cited By (8)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105668881A (en) * | 2016-03-16 | 2016-06-15 | 湖南京明环保科技有限公司 | Wastewater treatment system containing ammonia nitrogen |
| CN106746064A (en) * | 2015-11-24 | 2017-05-31 | 宜兴恒盛农业发展有限公司 | A kind of juice production water processing system |
| CN108706801A (en) * | 2018-07-23 | 2018-10-26 | 云南普发环境工程有限公司 | The ultraviolet device and method for strengthening ozone treatment country sewage is cooperateed with based on Hydrodynamic cavitation |
| CN108751344A (en) * | 2018-08-09 | 2018-11-06 | 孙鹏 | A kind of batch type processing system and treatment process of industrial wastewater middle and high concentration COD |
| CN109942153A (en) * | 2019-04-12 | 2019-06-28 | 张会 | A kind of High-concentration organic wastewater treatment method |
| CN111960523A (en) * | 2020-09-04 | 2020-11-20 | 浙江浙能技术研究院有限公司 | Method and device for realizing gas-water mixing and activating through secondary hydrodynamic cavitation and ultrasonic cavitation |
| CN112456700A (en) * | 2019-09-09 | 2021-03-09 | 广西精典化工新材料有限公司 | Wastewater treatment method for urea-formaldehyde resin and phenolic resin production enterprises |
| CN113562926A (en) * | 2021-07-27 | 2021-10-29 | 王娅娜 | Mariculture tail water treatment facilities |
-
2014
- 2014-08-12 CN CN201420451442.3U patent/CN204022606U/en not_active Expired - Fee Related
Cited By (11)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106746064A (en) * | 2015-11-24 | 2017-05-31 | 宜兴恒盛农业发展有限公司 | A kind of juice production water processing system |
| CN105668881A (en) * | 2016-03-16 | 2016-06-15 | 湖南京明环保科技有限公司 | Wastewater treatment system containing ammonia nitrogen |
| CN105668881B (en) * | 2016-03-16 | 2018-07-27 | 湖南京明环保科技有限公司 | Wastewater treatment system containing ammonia nitrogen |
| CN108706801A (en) * | 2018-07-23 | 2018-10-26 | 云南普发环境工程有限公司 | The ultraviolet device and method for strengthening ozone treatment country sewage is cooperateed with based on Hydrodynamic cavitation |
| CN108706801B (en) * | 2018-07-23 | 2023-05-23 | 云南普发工程咨询有限公司 | Device and method for treating rural sewage based on hydrodynamic cavitation and ultraviolet strengthening ozone |
| CN108751344A (en) * | 2018-08-09 | 2018-11-06 | 孙鹏 | A kind of batch type processing system and treatment process of industrial wastewater middle and high concentration COD |
| CN109942153A (en) * | 2019-04-12 | 2019-06-28 | 张会 | A kind of High-concentration organic wastewater treatment method |
| CN112456700A (en) * | 2019-09-09 | 2021-03-09 | 广西精典化工新材料有限公司 | Wastewater treatment method for urea-formaldehyde resin and phenolic resin production enterprises |
| CN111960523A (en) * | 2020-09-04 | 2020-11-20 | 浙江浙能技术研究院有限公司 | Method and device for realizing gas-water mixing and activating through secondary hydrodynamic cavitation and ultrasonic cavitation |
| CN111960523B (en) * | 2020-09-04 | 2023-12-12 | 浙江浙能技术研究院有限公司 | Method and device for realizing gas-water miscible activation through secondary hydrodynamic cavitation and ultrasonic cavitation |
| CN113562926A (en) * | 2021-07-27 | 2021-10-29 | 王娅娜 | Mariculture tail water treatment facilities |
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| Date | Code | Title | Description |
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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: 20141217 Termination date: 20190812 |