CN208700665U - A kind of advanced oxidation device - Google Patents
A kind of advanced oxidation device Download PDFInfo
- Publication number
- CN208700665U CN208700665U CN201821235762.XU CN201821235762U CN208700665U CN 208700665 U CN208700665 U CN 208700665U CN 201821235762 U CN201821235762 U CN 201821235762U CN 208700665 U CN208700665 U CN 208700665U
- Authority
- CN
- China
- Prior art keywords
- pipe
- ozone
- aeration cylinder
- aeration
- collector
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Active
Links
Abstract
The utility model relates to a kind of advanced oxidation devices, including treatment box, the first aeration cylinder of setting and the second aeration cylinder inside treatment box, collector is respectively provided with inside first aeration cylinder and the second aeration cylinder, ozone collection portion is respectively provided at the top of first aeration cylinder and the second aeration cylinder, the fixed several quartz burners in ozone collection portion bottom end, treatment box side is connected to water inlet pipe and outlet pipe, and the first suction inlet is arranged in water inlet pipe side, first suction inlet is connected to the first air dissolved pump, first air dissolved pump is connected to the first vacuum tube and first pipe, first pipe is connected to the first critical pipe, the other end of first critical pipe is through in the collector in the first aeration cylinder.The ozone for being included in Ozone Water is decomposed into hydrogen peroxide and OH radical ion, improves the capacity of decomposition of harmful substance hard-decomposed for refractory organic compounds and ammonia nitrogen etc. by utility model device transmitting UV in the Ozone Water of not bubbles.
Description
Technical field
The utility model relates to field of sewage treatment, and in particular to a kind of advanced oxidation device.
Background technique
As the continuous upgrading of industrial enterprise develops, there is three Gao Xianxiang, high salinity, high ammonia nitrogen, height in industrial wastewater
COD.Three high waste water are easy to cause microorganism to be poisoned, and biochemical method has been not suitable for.And some other processing means, such as wet process oxygen
Change, film process, burns, the technologies such as evaporation, the utilization due to the limitation in investment and operating cost, on Industrial Waste Water Treatments
It is all limited with acting on.
Fenton has been achieved for some preferable achievements as a kind of more extensive processing means of application now.However,
Although organic concentration can be effectively reduced in Fenton technology, its limited efficacy not can solve ammonia nitrogen problem, and salinity have compared with
Big promotion, and generate a large amount of materialized mud.
Utility model content
The purpose of this utility model is to provide a kind of advanced oxidation devices, to solve industrial wastewater in the prior art
The problems such as treatment effeciency is low.
The utility model provides a kind of advanced oxidation device, including treatment box, and setting first exposes inside the treatment box
Inflator and the second aeration cylinder, are respectively provided with collector inside first aeration cylinder and the second aeration cylinder, first aeration cylinder and
Ozone collection portion, the fixed several quartz burners in ozone collection portion bottom end, the purple are respectively provided at the top of second aeration cylinder
Outside line fluorescent tube is set to collector periphery, and the ozone collection portion on first aeration cylinder top connects ozone recovery tube, and described the
The ozone collection portion connection ozone collecting pipe on two aeration cylinder tops, the treatment box side connection water inlet pipe and outlet pipe, and into
The first suction inlet and the second suction inlet is arranged in water pipe side, and first suction inlet is connected to the first air dissolved pump, first air dissolved pump
It is connected to the first vacuum tube and first pipe, first vacuum tube is used to be the first air dissolved pump ozone supply, the first pipe
It is connected to the first critical pipe, the other end of the first critical pipe is through in the collector in the first aeration cylinder, second sucking
Mouth the second air dissolved pump of connection, the second air dissolved pump connection second pipe and ozone recovery tube, the second pipe connection second
The other end of critical pipe, the second critical pipe is through in the collector in the second aeration cylinder.
Further, it is respectively provided with monitor on first vacuum tube and ozone recovery tube, for monitoring the ozone in pipe
Concentration.
Further, hydraulic gage and sensor control valve, the hydraulic pressure are respectively provided on the first pipe and second pipe
Meter and the electrical connection of sensor control valve.
Further, first aeration cylinder and the second aeration cylinder periphery are respectively provided with water fender.
Further, discharge outlet is arranged in the collector bottom end.
Further, the diameter of the discharge outlet is 1.5cm.
Further, the ozone concentration supplied in first vacuum tube is 3%~12%.
Beneficial effect using above-mentioned technical solutions of the utility model is:
Utility model device transmitting UV in the Ozone Water of not bubbles decomposes the ozone for being included in Ozone Water
For hydrogen peroxide (H2O2) and OH radical ion, nuisance hard-decomposed for refractory organic compounds and ammonia nitrogen etc. can be improved as a result,
The capacity of decomposition of matter, and raw water can be handled in real time；
Utility model device reprocesses raw water using a small amount of residue ozone, does not need in addition to set
Residue ozone processing equipment is set, so environmental pollution can be prevented, hence it is evident that reduce cost of equipment and equipment maintenance cost.
Detailed description of the invention
Fig. 1 is the utility model advanced oxidation device structural schematic diagram；
Fig. 2 is the first aeration cylinder of the utility model structural schematic diagram；
In attached drawing, parts list represented by the reference numerals are as follows:
1- treatment box, the first aeration cylinder of 2-, the second aeration cylinder of 3-, 4- collector, 5- ozone collection portion, 6- ultraviolet radiator
Pipe, 7- ozone recovery tube, 8- ozone collecting pipe, 9- water inlet pipe, 10- outlet pipe, the first suction inlet of 11-, the second suction inlet of 12-,
The first air dissolved pump of 13-, the first vacuum tube of 14-, 15- first pipe, the critical pipe of 16- first, the second air dissolved pump of 17-, 18- second are managed
Road, the critical pipe of 19- second, 20- monitor, 21- hydraulic gage, 22- sensor control valve, 23- water fender, 24- discharge outlet.
Specific embodiment
It is practical new below in conjunction with this to keep the objectives, technical solutions, and advantages of the embodiments of the present invention clearer
Attached drawing in type embodiment, the technical scheme in the utility model embodiment is clearly and completely described, it is clear that is retouched
The embodiment stated is the utility model a part of the embodiment, instead of all the embodiments.
As shown in Figs. 1-2, the utility model provides a kind of advanced oxidation device, including treatment box 1, the treatment box 1
The first aeration cylinder 2 and the second aeration cylinder 3 is arranged in inside, is respectively provided with collector inside first aeration cylinder 2 and the second aeration cylinder 3
4, the top of first aeration cylinder 2 and the second aeration cylinder 3 is respectively provided with ozone collection portion 5, and 5 bottom end of ozone collection portion is fixed
Several quartz burners 6, the quartz burner 6 are set to 4 periphery of collector, and the ozone on 2 top of the first aeration cylinder is received
Collection portion 5 connects ozone recovery tube 7, and the ozone collection portion 5 on 3 top of the second aeration cylinder connects ozone collecting pipe 8, the processing
1 side of case is connected to water inlet pipe 9 and outlet pipe 10, and 9 side of water inlet pipe is arranged the first suction inlet 11 and the second suction inlet 12, and described the
One suction inlet 11 is connected to the first air dissolved pump 13, and first air dissolved pump 13 is connected to the first vacuum tube 14 and first pipe 15, described
First vacuum tube 14 is used to be 13 ozone supply of the first air dissolved pump, and the first pipe 15 is connected to the first critical pipe 16, and described the
The other end of one critical pipe 16 is through in the collector 4 in the first aeration cylinder 2, and second suction inlet 12 is connected to the second air dissolved pump
17, second air dissolved pump 17 is connected to second pipe 18 and ozone recovery tube 7, and the second pipe 18 is connected to the second critical pipe
19, the other end of the second critical pipe 19 is through in the collector 4 in the second aeration cylinder 3.It is untreated in the embodiment
Industrial wastewater enters in treatment box 1 through water inlet pipe 9, and industrial wastewater enters the first air dissolved pump 13, herein, work through the first suction inlet 11
Industry waste water is mixed with the ozone flowed into through the first vacuum tube 14, is flowed through the Ozone Water of the first air dissolved pump 13 and is gradually expanded flowing through
When neck, strong flow velocity is changed into pressure, makes mixed ozone dissolved under pressure, dissolved ozone be included in industrial wastewater
In oxidation material, organic substance reacted, carry out sterilization processing, then, mixed Ozone Water is through first pipe 15 and the
One critical pipe 16 flows into the collector 4 in the first aeration cylinder 2, wherein collector 4 is U-shaped structure, Ozone Water flow into after with receipts
Storage 4 collides, and is decomposed into small hydrone, meanwhile, it is mixed with unmixing ozone gas, the unmixing ozone gas bodily form
It is collected at bubble by the ozone collection portion 5 at 2 top of the first aeration cylinder, and is discharged by ozone recovery tube 7, Ozone Water is gradually upward
Mobile, the final Ozone Water for removing bubble flows downward between collector 4 and the first aeration cylinder 2, and is exposed to ultraviolet radiator
In the ultraviolet light that pipe 6 generates, the ozone for being exposed to ultraviolet light is reacted with water, using hydrogen peroxide as intermediate material, is formed
OH radical ion can dramatically speed up the processing speed including the harmful substances such as refractory organic compounds and ammonia nitrogen, and it is removed completely
It goes, the hydrogen peroxide being formed simultaneously can be decomposed into harmless water and oxygen；Simultaneously, the industry flowed into through water inlet pipe 9
Waste water also passes through the second suction inlet 12 and enters the second air dissolved pump 17, after industrial wastewater is mixed with the ozone that ozone recovery tube 7 flows into
It is flowed into the collector 4 in the second aeration cylinder 3 by second pipe 18 and the second critical pipe 19, specific handling principle is exposed with first
Working principle in inflator 2 is identical, and the water after processing most is flowed out through outlet pipe 10 afterwards.
It is respectively provided with monitor 20 on first vacuum tube 14 and ozone recovery tube 7, for monitoring the ozone concentration in pipe.
Hydraulic gage 21 and sensor control valve 22, the hydraulic gage are respectively provided in the first pipe 15 and second pipe 18
21 and sensor control valve 22 be electrically connected, when hydraulic gage 21 detect the hydraulic pressure in pipeline be more than reference range when, sensor control
Valve 22 processed is operated, and the operation of processing unit is automatically stopped.
Further, first aeration cylinder 2 and 3 periphery of the second aeration cylinder are respectively provided with water fender 23, so that discharge water arrives
Up to a certain amount of rear discharge.
Further, discharge outlet 24 is arranged in 4 bottom end of collector, and the diameter of the discharge outlet 24 is 1.5cm, nuisance
Matter is become gel-like the residue of object or solid matter outside 4 bottom of collector is discharged to by discharge outlet 24 after ozone treatment
Portion when 24 diameter of discharge outlet is 1.5 centimetres of bore, can also generate whirlpool in the inside of collector 4 even if not blocking discharge outlet 24
Stream, is automatically drained out gelling material or solid matter.
The ozone concentration supplied in first vacuum tube 14 is 3%~12%.
To sum up, utility model device transmitting UV in the Ozone Water of not bubbles will be included in the smelly of Ozone Water
Oxygen is decomposed into hydrogen peroxide (H2O2) and OH radical ion, it can be improved as a result, hard-decomposed for refractory organic compounds and ammonia nitrogen etc.
The capacity of decomposition of harmful substance, and raw water can be handled in real time.
Utility model device reprocesses raw water using a small amount of residue ozone, does not need in addition to set
Residue ozone processing equipment is set, so environmental pollution can be prevented, hence it is evident that reduce cost of equipment and equipment maintenance cost.
Finally, it should be noted that the above various embodiments is only to illustrate the technical solution of the utility model, rather than it is limited
System；Although the present invention has been described in detail with reference to the aforementioned embodiments, those skilled in the art should
Understand: it is still possible to modify the technical solutions described in the foregoing embodiments, or to some or all of
Technical characteristic is equivalently replaced；And these are modified or replaceed, it does not separate the essence of the corresponding technical solution, and this is practical new
The range of each embodiment technical solution of type.
Claims (7)
1. a kind of advanced oxidation device, which is characterized in that including treatment box, the first aeration cylinder of setting and the inside the treatment box
Two aeration cylinders are respectively provided with collector, first aeration cylinder and the second aeration inside first aeration cylinder and the second aeration cylinder
The top of cylinder is respectively provided with ozone collection portion, the fixed several quartz burners in ozone collection portion bottom end, the quartz burner
It is set to collector periphery, the ozone collection portion on first aeration cylinder top connects ozone recovery tube, second aeration cylinder
The ozone collection portion on top connects ozone collecting pipe, the treatment box side connection water inlet pipe and outlet pipe, and water inlet pipe side is set
The first suction inlet and the second suction inlet are set, first suction inlet is connected to the first air dissolved pump, the first air dissolved pump connection first
Vacuum tube and first pipe, first vacuum tube are used to be the first air dissolved pump ozone supply, the first pipe connection first
The other end of critical pipe, the first critical pipe is through in the collector in the first aeration cylinder, second suction inlet connection the
Two air dissolved pumps, the second air dissolved pump connection second pipe and ozone recovery tube, the second pipe are connected to the second critical pipe, institute
The other end for stating the second critical pipe is through in the collector in the second aeration cylinder.
2. advanced oxidation device according to claim 1, which is characterized in that on first vacuum tube and ozone recovery tube
It is respectively provided with monitor, for monitoring the ozone concentration in pipe.
3. advanced oxidation device according to claim 1, which is characterized in that be all provided on the first pipe and second pipe
Set hydraulic gage and sensor control valve, the hydraulic gage and the electrical connection of sensor control valve.
4. advanced oxidation device according to claim 1, which is characterized in that outside first aeration cylinder and the second aeration cylinder
Week is respectively provided with water fender.
5. advanced oxidation device according to claim 1, which is characterized in that discharge outlet is arranged in the collector bottom end.
6. advanced oxidation device according to claim 5, which is characterized in that the diameter of the discharge outlet is 1.5cm.
7. advanced oxidation device according to claim 1, which is characterized in that the ozone supplied in first vacuum tube is dense
Degree is 3%~12%.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201821235762.XU CN208700665U (en) | 2018-08-02 | 2018-08-02 | A kind of advanced oxidation device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201821235762.XU CN208700665U (en) | 2018-08-02 | 2018-08-02 | A kind of advanced oxidation device |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN208700665U true CN208700665U (en) | 2019-04-05 |
Family
ID=65940326
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201821235762.XU Active CN208700665U (en) | 2018-08-02 | 2018-08-02 | A kind of advanced oxidation device |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN208700665U (en) |
-
2018
- 2018-08-02 CN CN201821235762.XU patent/CN208700665U/en active Active
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN205258222U (en) | Sewage treatment device | |
| CN107381918A (en) | A kind of sewage disposal and retracting device | |
| CN208700665U (en) | A kind of advanced oxidation device | |
| CN206437986U (en) | A kind of sound, light, ozone coupling handle the device of organic wastewater | |
| CN105198184A (en) | Low-energy-consumption low-odor deep-dehydration method for sludge in sewage treatment plant | |
| CN207493492U (en) | A kind of VOCs biological treatment devices | |
| CN203754540U (en) | Industrial sewage treatment equipment | |
| CN212894002U (en) | Sewage treatment system | |
| CN206373158U (en) | A kind of two-phase ozone-ultraviolet photocatalysis repair system for organic contamination soil | |
| CN206350983U (en) | A kind of efficient organic waste gas treatment device | |
| KR20020043513A (en) | Multiple drying system of sludge using microwave | |
| CN208500567U (en) | Rare Earth Separation processing waste water processing equipment | |
| CN113060876A (en) | Air-flotation ultrafiltration treatment system and process for ship tail gas desulfurization washing wastewater | |
| CN207056299U (en) | Waste gas purification apparatus in a kind of chemical plant | |
| CN211990239U (en) | Multiphase extraction coupling recharge processing system | |
| CN204737817U (en) | Heavy metal wastewater treatment facility | |
| CN212476329U (en) | Device of greasy dirt on water is retrieved in high efficiency separation | |
| CN213803381U (en) | Synthesize waste water treatment in-process waste gas collection processing apparatus that volatilizees | |
| CN214734632U (en) | Chemical reaction effluent treatment plant | |
| CN218107239U (en) | Multiphase extraction equipment | |
| CN214244121U (en) | Circulating well system for in-situ remediation of organic polluted underground water | |
| CN220745596U (en) | Leachate contaminated sludge treatment equipment | |
| CN215782633U (en) | Ozone tail gas treatment system | |
| CN214130935U (en) | Waste gas treatment device for sewage treatment with good treatment effect | |
| CN208120886U (en) | One kind is containing the leaded wastewater efficient processing unit of acid |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| GR01 | Patent grant | ||
| GR01 | Patent grant |